METHOD OF EMULSION CONCENTRATION OPTIMIZATION FOR COLD CONTINUOUS ROLLING MILL SET

Abstract

Disclosed is a method of emulsion concentration optimization for a cold continuous rolling mill set for achieving vibration suppression, the method comprising: defining the process parameters involved in the process of emulsion concentration optimization; setting an initial set value of an emulsion concentration comprehensive optimization target function for a cold continuous rolling mill set for achieving vibration suppression; calculating a bite angle of each stand; calculating a vibration determination index reference value of each stand; setting the emulsion concentration of each stand; calculating the outlet temperature of a strip steel of each stand; calculating the dynamic viscosity of an emulsion in a roll gap of each stand; calculating the oil film thickness in the roll gap of each stand; calculating the emulsion concentration comprehensive optimization target function; determining whether the inequation F(X)

Description

TECHNICAL FIELD

The present invention belongs to the field of cold continuous rolling, and in particular relates to a method of emulsion concentration optimization for a cold continuous rolling mill set for achieving vibration suppression.

BACKGROUND

As an important process parameter in the process lubrication system, emulsion concentration plays a vital role in the lubrication status of the roll gap of each stand of the cold continuous rolling mill set.

At the same time, the lubrication status of the roll gap directly affects the occurrence of vibration defects of the rolling mill.

If the roll gap is in an over-lubricated status, the friction coefficient is too small, which is likely to cause slip in the rolling process and leads to self-excited vibration of the rolling mill. If the roll gap is in an under-lubricated status, the average oil film thickness in the roll gap is less than the required minimum value, which is likely to cause the oil film in the roll gap to crack during the rolling process and leads to the sharp increase of the friction coefficient, thus changing the rolling pressure, causing the periodic fluctuation of the system stiffness and causing the self-excited vibration of the rolling mill as well.

In the past, the site generally relies on the speed of the rolling mill to suppress the occurrence of vibration defects, but this operation restricts the improvement of the production efficiency of the cold continuous rolling mill set and seriously affects the economic benefits of the enterprise.

The Chinese invention patent with the authorized announcement number of CN 103544340 B and the authorized announcement date of Mar. 2, 2016 discloses a “Method for Setting Emulsion Concentration in Extremely Thin Strip Rolling of Five-stand Cold Continuous Rolling Mill Set”. The method for setting emulsion concentration includes the following steps executed by a computer: 1) acquiring the main equipment of the mill set, the characteristics of the strip to be rolled, the main rolling process and the process lubrication system parameters; 2) defining relevant process parameters; 3) calculating the roll bending force and roll shifting amount; 4) assigning values to relevant search process parameters; 5) calculating concentration process parameters; 6) calculating the search process speed of the maximum rolling speed; 7) calculating the friction coefficient of each stand under the current conditions; 8) calculating the rolling force, rolling power, slip factor, thermal slip injury index and vibration coefficient of each stand under the current conditions; 9) calculating the thermal crown of the work roll of each stand; 10) calculating the outlet plate shape and the forced-contact width; and 11) obtaining and outputting the optimum proportion concentration. It can be seen that the patent aims at improving the rolling speed, ensuring the rolling efficiency, and avoiding slipping, thermal slip injury and vibration, so as to ensure the outlet plate shape of the final stand and the minimum forced-contact width at the work roll end.

Through research, it is found that under the premise of determining the process parameters such as rolling schedule, roll process, emulsion flow rate and initial temperature, the setting of emulsion concentration directly determines the lubrication status of the roll gap of each stand of the cold continuous rolling mill set, and can be used as the main process control means to suppress the vibration of the rolling mill.

However, at present, there has not been a report providing the technical solution of suppressing the vibration of the rolling mill by changing the previous mode of constant concentration control of an emulsion in each stand and taking the concentration of the emulsion in each stand as a variable to be optimized.

SUMMARY

The technical problem to be solved by the invention is to provide a method of emulsion concentration optimization for a cold continuous rolling mill set for achieving vibration suppression. The method changes the previous mode of constant concentration control of the emulsion in each stand, takes the concentration of the emulsion in each stand as a variable to be optimized, and carries out comprehensive optimization control on emulsion concentration. The lubrication status of roll gaps in each stand is optimized through the reasonable proportion of emulsion concentration in each stand, thus achieving the purposes of suppressing vibration of the rolling mill, improving product quality and production efficiency, and bringing economic benefits to enterprises.

The technical solution of the invention is to provide a method of emulsion concentration optimization for a cold continuous rolling mill set for achieving vibration suppression, wherein the method includes the following steps:

(a) acquiring apparatus characteristic parameters of a cold continuous rolling mill set;

(b) acquiring critical rolling process parameters of a strip material;

(c) acquiring process parameters involved in the process of emulsion concentration optimization;

(d) setting an initial set value F₀=1.0×10¹⁰ of an emulsion concentration comprehensive optimization target function for a cold continuous rolling mill set for achieving vibration suppression;

the executing order of steps (a) to (d) is not limited;

(e) calculating a bite angle α_i of each stand;

(f) calculating a vibration determination index reference value ξ_0i of each stand;

(g) setting an emulsion concentration C_i of each stand;

(h) calculating the outlet temperature T_i of a strip steel of each stand;

(i) calculating the dynamic viscosity η_0i of an emulsion in a roll gap of each stand;

(j) calculating an oil film thickness ξ_i in the roll gap of each stand;

(k) calculating the emulsion concentration comprehensive optimization target function F(X);

(l) determining whether the inequation F(X)<F₀, is established, if yes, then setting C_i^y=C_i, F₀=F(X) and turning to step (m); if no, directly turning to step (m);

(m) determining whether the emulsion concentration C_i exceeds the range of a feasible region, if yes, turning to step (n); if no, turning to the step (g); wherein the feasible region refers to a region from 0 to the maximum emulsion concentration allowed by an apparatus, and wherein the allowed emulsion concentration of the apparatus is usually within 10%, and 0˜10% can be set as the feasible range;

(n) outputting the optimal emulsion concentration set value C_i^y, wherein C_i^y is the value of C_i when the calculated value of F(X) is minimum in the feasible region; and

(o) adjusting and controlling the emulsion concentration of each stand according to the optimal emulsion concentration set value C_i^y in the step (n) by a control system of the cold continuous rolling mill set.

wherein calculating the vibration determination index reference value ξ_0i of each stand in the step (f) comprising the following steps:

(f1) calculating an over-lubricated oil film thickness critical value ξ_i⁺ of each stand as follows:

it is assumed that when

$\frac{{\gamma }_i}{{\alpha }_i}=A^{+},$

the roll gap is just in an over-lubricated status, wherein γ_i is a neutral angle of each stand, and A⁺ is an over-lubricated determining coefficient;

calculating to obtain

$u_i^{+}=\frac{1}{2\left(2A^{+}-1\right)}\left(\sqrt{\frac{\Delta h_i}{{R_i}^{\prime }}}+\frac{T_{i0}-T_{i1}}{P_i}\right)$

according to

${\alpha }_i=\sqrt{\frac{\Delta h_i}{{R_i}^{\prime }}},$

wherein Δh_i is the rolling reduction, Δh_i=h_0i−h_1i, h_0i is the inlet thickness of each stand, h_1i is the outlet thickness of each stand, and R_i′ is the flattening radius of a work roll of the i^th stand,

and

${\gamma }_i=\frac{1}{2}\sqrt{\frac{\Delta h_i}{{R_i}^{\prime }}}\left[1+\frac{1}{2u_i}\left(\sqrt{\frac{{\Delta h}_i}{{R_i}^{\prime }}}+\frac{T_{i0}-T_{i1}}{P_i}\right)\right]$

wherein T_0i is the back tension of each stand, T_1i is the front tension of each stand, and P_i is the rolling pressure of each stand,

according to the relationship between the friction coefficient and the oil film thickness: u_i=a_i+b_i·e^Hi·ξi, wherein a_i is the liquid friction influence coefficient, b_i is the dry friction influence coefficient, and B_i is the friction coefficient attenuation index, the over-lubricated oil film thickness critical value ξ_i⁺ of each stand is calculated by:

${\xi }_i^{+}=\frac{1}{B_i}\ln \frac{u_i^{+}-a_i}{b_i};$

(f2) calculating an under-lubricated oil film thickness critical value ξ_i⁻ of each stand as follows:

it is assumed that when

$\frac{{\gamma }_i}{{\alpha }_i}=A^{-},$

the roll gap is just in an under-lubricated status, wherein A⁻ is the under-lubricated determining coefficient, the following equation can be obtained:

$u_i^{-}=\frac{1}{2\left(2A^{-}-1\right)}\left(\sqrt{\frac{\Delta h_i}{R_i^{\prime }}}+\frac{T_{i0}-T_{i1}}{P_i}\right);$

and the under-lubricated oil film thickness critical value ξ_i⁻ of each stand is calculated by:

${\xi }_i^{-}=\frac{1}{B_i}\ln \frac{u_i^{-}-a_i}{b_i};$

and

(f3) calculating the vibration determination index reference value ξ_0i of each stand as follows:

${\xi }_{0i}=\frac{{\xi }_i^{+}+{\xi }_i^{-}}{2}.$

wherein calculating the outlet temperature T_i of the strip steel of each stand in the step (h) comprising the following steps:

(h1) calculating the outlet temperature T₁ of the first stand:

$T_1=T_1^{\mathrm{Inlet}}+\frac{1-\left({\varepsilon }_1/4\right)}{1-\left({\varepsilon }_1/2\right)}·\frac{K_1\ln \left(\frac{1}{1-{\varepsilon }_1}\right)}{pSJ},$

wherein T₁^inlet is the inlet temperature of each stand,

${\varepsilon }_i=\frac{\Delta h_i}{h_{0i}},$

Δh_i=h_0i−h_1i, h_0i is the inlet thickness of each stand, h_1i is the outlet thickness of each stand, ρ is the density of strip steel, S is the specific heat capacity of strip steel, J is the mechanical equivalent of heat, and K_i is the resistance to deformation of the strip steel of each stand;

(h2) setting i to 1;

(h3) setting the temperature of the first section of strip steel behind the outlet of the i^th stand to T_{i, 1}, i.e., T_{i, 1}=T_i;

(h4) setting j to 2;

(h5) the relationship between the temperature of the j^th section and the temperature of the j−1^th section satisfies the following equation:

$T_{i,j}=-\frac{2k_0{w}^{0.264}\exp \left(9.45-0.1918C_i\right)\times 1.163l}{v_{1i}{h}_{1i}\rho Sm}{T}_{i,j-1}^{-0.213}\left(T_{i,j-1}-T_c\right)+T_{i,j-1},$

wherein k₀ is the influence coefficient of nozzle shape and spraying angle, 0.8<k₌₀<1.2, w is the flow rate of the emulsion, l is the distance between stands, and the distance l between stands is equally divided into m sections, the temperature in the section is represented by T_{i, j}, v_1i is the outlet speed of each stand, h_1i is the outlet thickness of each stand, ρ is the density of the strip steel, S is the specific heat capacity of the strip steel, T_i is the outlet temperature of each stand, and T_c is the temperature of the emulsion;

(h6) determining whether the inequation j<m is established, if yes, then setting j=j+1 and turning to the step (h5); if no, turning to step (h7);

(h7) obtaining the temperature T_i,m of the m^th section via iterative calculation;

(h8) calculating the inlet temperature T_i+1^Inlet of the i+1^th stand:

T _i+1 ^Inlet =T _i,m;

(h9) calculating the outlet temperature T_i+1 of the i+1′ stand;

$T_{i+1}=T_{i+1}^{\mathrm{Inlet}}+\frac{1-\left({\varepsilon }_{i+1}/4\right)}{1-\left({\varepsilon }_{i+1}/2\right)}·\frac{K_{i+1}\ln \left(\frac{1}{1-{\varepsilon }_{i+1}}\right)}{\rho \mathrm{SJ}};$

(h10) determining whether the inequation i<n is established, if yes, setting i=i+1 and turning to the step (h3); if no, turning to step (h11); and

(h11) obtaining the outlet temperature T_i of each stand.

Specifically, apparatus characteristic parameters of the cold continuous rolling mill set at least include:

the radius R_i of a work roll of each stand; the surface linear speed v_ri of a roll of each stand; the original roughness Ra_ir0 of a work roll of each stand; the roughness attenuation coefficient B_L, of a work roll; the distance l between stands; and rolling kilometers L_i of a work roll of each stand after roll change; wherein i=1, 2, . . . , n; i represents the ordinal number of the stand of the cold continuous rolling mill set, and n is the total number of the stands.

Specifically, the critical rolling process parameters of the strip material at least include:

the inlet thickness h_0i of each stand; the outlet thickness h_1i of each stand; the width B of the strip steel; the inlet speed v_0i of each stand; the outlet speed v_1i of each stand; the inlet temperature T₁^Inlet; the resistance to deformation K_i of the strip steel of each stand; the rolling pressure P_i of each stand; the back tension T_0i of each stand; the front tension T₁₁ of each stand; the concentration influence coefficient k_c of the emulsion; the viscosity compression coefficient θ of a lubricant; the density ρ of the strip steel; the specific heat capacity S of the strip steel; the flow rate w of the emulsion; the temperature T_c of the emulsion; and the mechanical equivalent of heat J.

Specifically, the process parameters involved in the process of emulsion concentration optimization at least include: the over-lubricated oil film thickness critical value ξ_i⁺ and the corresponding friction coefficient u_i⁺ of each stand; the under-lubricated oil film thickness critical value ξ_i⁻ and the corresponding friction coefficient u_i⁻ of each stand; the vibration determination index reference value ξ_0i; the rolling reduction Δh_i=h_0i−h_1i; the rolling reduction ratio

${\varepsilon }_i=\frac{\Delta h_i}{h_{0i}};$

the inlet temperature T_i^Inlet of each stand; and the outlet temperature T_i of each stand; the distance l between stands, which is equally divided into m sections, the temperature in the section represented by T_{i, j}, wherein 1≤j≤m and T_i^Inlet=T_i−1,m; the over-lubricated determining coefficient A⁺; and the under-lubricated determining coefficient A⁻.

Further, the calculation formula for calculating the bite angle α_i of each stand is as follows:

${\alpha }_i=\sqrt{\frac{\Delta h_i}{R_i^{\prime }}}$

wherein R_i′ is the flattening radius of the work roll of the i^th stand, and is a process value in rolling pressure calculation.

Further, the calculation formula for calculating the dynamic viscosity η_0i of the emulsion in the roll gap of each stand is as follows:

η_0i=b·exp(−a·T_i)

wherein a and b are dynamic viscosity parameters of the lubricant under atmospheric pressure.

Further, the calculation formula for calculating the oil film thickness ξ_i in the roll gap of each stand is as follows:

${\xi }_i=\frac{h_{0i}+h_{1i}}{2h_{0i}}·k_c·\frac{3\theta {\eta }_{0i}\left(v_{\mathrm{ri}}+v_{0i}\right)}{{\alpha }_i\left[1-e^{-\theta \left(K_i-\frac{T_{0i}}{h_{0i}·B}\right)}\right]}-k_{\mathrm{rg}}·\left(1+K_{\mathrm{rs}}\right)·{\mathrm{Ra}}_{\mathrm{ir}0}·e^{-B_{\mathrm{Li}}·L_i},$

wherein h_0i is the inlet thickness of each stand, h_1i is the outlet thickness of each stand, k_c is the emulsion concentration influence coefficient, θ is the viscosity compression coefficient of the lubricant, K_i is the resistance to deformation of the strip steel of each stand, η_0i is the dynamic viscosity of the emulsion in the roll gap of each stand, v_0i is the inlet speed of each stand, v_ri is the surface linear speed of a roll of each stand, T_0i is the back tension of each stand, B is the width of the strip steel, k_rg represents the coefficient of the strength of the surface longitudinal roughness of the work roll and the strip steel to entrain the lubricant, the value of which is from 0.09 to 0.15, K_rs represents the impression rate, i.e., the ratio of transmitting surface roughness of the work roll to the strip steel, the value of which is from 0.2 to 0.6, Ra_ir0 is the original roughness of a work roll of each stand, B_L is the roughness attenuation coefficient of the work roll, and L_i is the rolling kilometers of a work roll of each stand after roll change.

Further, the emulsion concentration comprehensive optimization target function is calculated according to the following formula:

$\{\begin{array}{c}F\left(X\right)=\frac{\lambda }{n}\sum _{i=1}^n\sqrt{{\left({\xi }_i-{\xi }_{0i}\right)}^2}+\left(1-\lambda \right)\max {\zeta }_i-{\xi }_{0i}\\ {\xi }_i^{-}<{\xi }_i<{\xi }_i^{+}\end{array},$

wherein x={C_i} is an optimized variable, and λ is a distribution coefficient.

In the disclosure, as long as the execution of the next step is not conditional on the result of the previous step, it is not necessary to proceed according to the above order, unless the execution of the next step depends on the previous step.

Compared with the prior art, the invention has the following advantages:

1. The lubricated status of roll gaps in each stand is optimized through reasonable proportion of the emulsion concentration of each stand, thus achieving the purposes of suppressing vibration of the rolling mill, and improving product quality and production efficiency.

2. As a result of a large number of field tests and theoretical research, based on the apparatus characteristics and rolling process features of the cold continuous rolling mill set, a method of emulsion concentration optimization for a cold continuous rolling mill set for achieving vibration suppression is put forward. The method realizes the optimal ratio of emulsion concentration for each stand of the cold continuous rolling mill set, achieves suppressing vibration of the rolling mill and improving product quality and production efficiency, and brings great economic benefits to enterprises.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a schematic flow diagram of the general technical solutions according to the present invention;

FIG. 2 is a schematic diagram of the calculation process of the reference value of the vibration determination index according to the present invention; and

FIG. 3 is a schematic diagram of the calculation process of the strip steel outlet temperature of each stand according to the present invention.

DETAILED DESCRIPTION

The invention will be further described below in conjunction with the accompany drawings and embodiments.

In order to further explain the application process of the related technologies mentioned in the invention, a 1730 cold continuous rolling mill set of a cold rolling plant is taken as an example. The application process of the method of emulsion concentration optimization for a cold continuous rolling mill set for achieving vibration suppression is described in detail.

At first, according to the various steps shown in FIG. 1, the relevant parameters are determined in turn. Then the parameters are substituted into corresponding formulas for calculation, and the desired optimal emulsion concentration set value C_i^y is determined or obtained. Finally, the emulsion concentration of each stand is controlled according to the determined optimal emulsion concentration set value, and the comprehensive optimization control is carried out to achieve suppressing the vibration of the rolling mill.

Specifically, in the step (a), the acquired apparatus characteristic parameters of a cold continuous rolling mill set mainly include:

the radius of a work roll of each stand: R_i={210, 212, 230, 230, 228} mm;

the surface linear speed of a roll of each stand: v_ri={180, 320, 500, 800, 1150} m/min;

the original roughness of a work roll of each stand: Ra_ir,0={1.0, 1.0, 0.8, 0.8, 1.0} um;

the roughness attenuation coefficient of the work roll: B_L=0.01;

the distance between stands: l=2700 mm; and

the rolling kilometers of a work roll of each stand after roll change: L_i={100, 110, 230, 180, 90} km; wherein i=1, 2, . . . , n; i represents the ordinal number of the stand of the cold continuous rolling mill set; and n=5, which is the total number of the stands, the same below;

subsequently, in the step (b), the acquired critical rolling process parameters of the strip material mainly include:

the inlet thickness of each stand: h_0i={2.0, 1.14, 0.63, 0.43, 0.28} mm;

the outlet thickness of each stand: h_1i˜={1.14, 0.63, 0.43, 0.28, 0.18} mm;

the width of the strip steel: B=966 mm;

the inlet speed of each stand: v_0i={110, 190, 342, 552, 848} m/min;

the outlet speed of each stand: v_1i={190, 342, 552, 848, 1214} m/min;

the inlet temperature: T₁^Inlet=10° C.;

the resistance to deformation of the strip steel of each stand:

K_i={36, 40, 480, 590, 650} MPa;

the rolling pressure of each stand: P_i={12800, 11300, 10500, 9600, 8800} kN;

the back tension of each stand: T_0i={70, 145, 208, 202, 229} MPa;

the front tension of each stand: T_1i={145, 208, 202, 229, 56} MPa;

the concentration influence coefficient of the emulsion: k_c=0.9;

the viscosity compression coefficient of the lubricant: θ=0.034;

the density of the strip steel: ρ=7800 kg/m³;

the specific heat capacity of the strip steel: S=0.47 kJ/(kg·° C.);

the flow rate of the emulsion: w=900 m/min;

the temperature of the emulsion: T_c=58° C.;

the mechanical equivalent of heat: J=1; and

the flattening radius of the work roll of the it stand: R_i′={278.2, 279.7, 300.5, 301.6, 295.4};

subsequently, in the step (c), the acquired process parameters involved in the process of emulsion concentration optimization mainly include: the over-lubricated oil film thickness critical value ξ_i⁺ and the corresponding friction coefficient u_i⁺ of each stand; the under-lubricated oil film thickness critical value ξ_i⁻ and the corresponding friction coefficient u_i⁻ of each stand; the vibration determination index reference value ξ_0i, the rolling reduction: Δh_i=h_0i−h_1i={0.86, 0.51, 0.2, 0.15, 0.1}; the rolling reduction ratio:

${\varepsilon }_i=\frac{\Delta h_i}{h_{0i}}=\left\{0.43,0.45,0.32,0.35,0.36\right\};$

the inlet temperature T_i^Inlet each stand; and the outlet temperature T_i of each stand; the distance l between stands is 2700 mm, which is equally divided into m=30 sections, the temperature in the section is represented by T_{i, j} (wherein 1≤j≤m), and T_i^Inlet=T_i−1,m; the over-lubricated determining coefficient A⁺; and the under-lubricated determining coefficient A⁻.

subsequently, in the step (d), an initial set value F₀=1.0×10¹⁰ of an emulsion concentration comprehensive optimization target function for a cold continuous rolling mill set for achieving vibration suppression is set;

subsequently, in the step (e), the bite angle α_i of each stand is calculated according to the rolling theory using the calculation formula:

${\alpha }_i=\sqrt{\frac{\Delta h_i}{R_i^{\prime }}},$

obtaining α_i={0.0556, 0.0427, 0.0258, 0.0223, 0.0184};

subsequently, in the step (f), the vibration determination index reference value ξ_0i of each stand is calculated according to the sub-steps shown in the FIG. 2:

(f1) calculating the over-lubricated oil film thickness critical value ξ_i⁺ of each stand:

it is assumed that when

$\frac{{\gamma }_i}{{\alpha }_i}=A^{+}=1,$

the roll gap is just in an over-lubricated status; according to

${\alpha }_i=\sqrt{\frac{\Delta h_i}{{R_i}^{\prime }}}$

and the calculation formula of the neutral angle γ_i of each stand,

$u_i^{+}=\frac{1}{2\left(2A^{+}-1\right)}\left(\sqrt{\frac{{\Delta h}_i}{{R_i}^{\prime }}}+\frac{T_{i0}-T_{i1}}{P_i}\right)$

is obtained, obtaining u_i⁺={00248, 0.0186, 0.0132, 0.0136, 0.0191};

according to the relationship between the friction coefficient and the oil film thickness: u_i=a_i+b_i·e^Bi·ξi (in the embodiment, a_i=0.0126, b_i=0.1416, and B_i=−2.4297), the over-lubricated oil film thickness critical value ξ_i⁺ of each stand is calculated by the calculation formula:

${\xi }_i^{+}=\frac{1}{B_i}\ln \frac{u_i^{+}-a_i}{b_i},$

obtaining ξ_i⁺={1.009, 1.301, 2249, 2.039, 1.268} um;

(f2) calculating the under-lubricated oil film thickness critical value ξ_i⁺ of each stand is calculated:

it is assumed that when

$\frac{{\gamma }_i}{{\alpha }_i}=A^{-}=0.6,$

the roll gap is just in an under-lubricated status,

$u_i^{-}=\frac{1}{2\left(2A^{-}-1\right)}\left(\sqrt{\frac{{\Delta h}_i}{{R_i}^{\prime }}}+\frac{T_{i0}-T_{i1}}{P_i}\right),$

u_i⁻={0.1240, 0.0930, 0.0660, 0.0680, 0.0955};

according to the relationship between the friction coefficient and the oil film thickness: u_i=a_i+b_i·e^Bi·ξi, the under-lubricated oil film thickness critical value ξ_i⁻ of each stand is calculated by the calculation formula

${\xi }_i^{-}=\frac{1}{B_i}\ln \frac{u_i^{-}-a_i}{b_i},$

obtaining ξ_i⁻={0.098, 0.233, 0.401, 0.386, 0.220} um;

subsequently, in the step (f3), the vibration determination index reference value ξ_0i is calculated, wherein

${\xi }_{0i}=\frac{{\xi }_i^{+}+{\xi }_i^{-}}{2},$

obtaining ξ_0i={0.554, 0.767, 1.325, 1.213, 0.744};

subsequently, in the step (g), the emulsion concentration of each stand is set as C_i={4.2, 4.2, 4.2, 4.2, 4.2} %.

Then, in the step (h), the outlet temperature T_i of the strip steel of each stand is calculated according to the sub-steps shown in the FIG. 3.

Subsequently, in the step (h1), the outlet temperature T₁ of the first stand is calculated as follows:

$T_1=T_1^{\mathrm{Inlet}}+\frac{1-\left({\varepsilon }_1/4\right)}{1-\left({\varepsilon }_1/2\right)}·\frac{K_1\ln \left(\frac{1}{1-{\varepsilon }_1}\right)}{\rho \mathrm{SJ}}=110+\frac{1-(0.4\text{3/4)}}{1-(0.4\text{3/2)}}·\frac{360\ln \left(\frac{1}{1-0.43}\right)}{7.8·0.47·1}=172.76°C.$

Subsequently, in the step (h2), i is set to 1.

Subsequently, in the step (h3), the temperature of the first section of strip steel behind the outlet of the f0 stand is set to T_{i, 1}, i.e., T_{i, 1}=T_i=172.76° C.

Subsequently, in the step (h4), j is set to 2.

Subsequently, in the step (h5), the relationship between the temperature of the j^th section and the temperature of the j−1^th section satisfies the following equation:

$T_{i,j}=-\frac{2k_0{w}^{0.264}\exp \left(9.45-0.1918C_i\right)\times 1.163l}{v_{1i}{h}_{1i}\rho \mathrm{Sm}}{T}_{i,j-1}^{-0.213}\left(T_{i,j-1}-T_c\right)+T_{i,j-1},$

wherein k₀ is the influence coefficient of the nozzle shape and the spraying angle, and k₀=1.

Subsequently, in the step (h6), whether the inequation j<m is established is determined, if yes, then setting j=j+1 and turning to step (h5); if no, turning to step (h7).

Subsequently, in the step (h7), the temperature of the 30th section (when m=30) is obtained via iterative calculation: T_1.30=103.32° C.

Subsequently, in the step (h8), the inlet temperature T₂^Inlet of the second stand is calculated as follows: T₂^Inlet=T_1,m=103.32° C.

Subsequently, in the step (h9), the outlet temperature T₂ of the second stand is calculated as follows:

$T_2=T_2^{\mathrm{Inlet}}+\frac{1-\left({\varepsilon }_2/4\right)}{1-\left({\varepsilon }_2/2\right)}·\frac{K_2\ln \left(\frac{1}{1-{\varepsilon }_2}\right)}{\rho \mathrm{SJ}}=103.32+\frac{1-\left(0.4\text{5/4}\right)}{1-\left(0.4\text{5/2}\right)}·\frac{400\ln \left(\frac{1}{1-0.45}\right)}{7800·0.47·1}=178.02^{o}C.$

Subsequently, in the step (h10), whether the inequation i<n is established is determined; if yes, setting i=i+1 and turning to the step (h3); if no, turning to step (h11).

Subsequently, in the step (h11), the outlet temperature of each stand is obtained: T_i={17276, 17802, 186.59, 194.35, 206.33}° C.

Subsequently, in the step (i), the dynamic viscosity η_0i of the emulsion in the roll gap of each stand is calculated by equation: η_0i=b·exp(−a·T_i) (in the equation, a and b are dynamic viscosity parameters of the lubricant under the atmospheric pressure, wherein a=0.05, b=2.5), η_0i={5.39, 5.46, 5.59, 5.69, 5.84} is obtained.

Subsequently, in the step (j), the thickness ξ_i of the oil film in the roll gap of each stand is calculated by the following calculation formula:

${\xi }_i=\frac{h_{0i}+h_{1i}}{2h_{0i}}·k_c·\frac{3\theta {\eta }_{0i}\left(v_{\mathrm{ri}}+v_{0i}\right)}{{\alpha }_i\left[1-e^{-\theta \left(K_i\frac{T_{0i}}{h_{0i}·B}\right)}\right]}-k_{\mathrm{rg}}·\left(1+K_{\mathrm{rs}}\right)·{\mathrm{Ra}}_{\mathrm{ir0}}·e^{-B_{\mathrm{Li}}·L_i},$

wherein, k_rg represents the coefficient of the strength of the surface longitudinal roughness of the work roll and the strip steel to entrain the lubricant, wherein k_rg=1.183, K_rs represents the impression rate, i.e., the ratio of transmitting surface roughness of the work roll to the strip steel, wherein K_rs=0.576, and S={0.784, 0.963, 2.101, 2.043, 1.326} um is obtained.

Subsequently, in the step (k), the emulsion concentration comprehensive optimization target function is calculated as follows:

$\{\begin{array}{c}F\left(X\right)=\frac{\lambda }{n}\sum _{i=1}^n\sqrt{{\left({\xi }_i-{\xi }_{0i}\right)}^2}+\left(1-\lambda \right)\max \left|{\xi }_i-{\xi }_{0i}\right|\\ {\xi }_i^{-}<{\xi }_i<{\xi }_i^{+}\end{array};$

wherein X={C_i} is an optimized variable, and λ=0.5 is a distribution coefficient, and F(X)=0.94 is obtained.

Subsequently, in the step (1), if the equation, F(X)=0.94<F₀=1×10¹⁰, is established, then C_i^y=C_i={4.2, 4.2, 4.2, 4.2, 4.2} %, F₀=F(X)=0.94, and step (m) is performed.

Subsequently, in the step (m), whether the emulsion concentration C_i exceeds the range of the feasible region is determined, if yes, the step (n) is performed; if no, the step (g) is performed.

Subsequently, in the step (n), the optimal emulsion concentration set value C_i^y={4.2, 4.2, 4.5, 4.6, 4.3} % is outputted, wherein C_i^y is the value of C_i when the calculated value of F(X) is minimum in the feasible region.

Finally, during the whole rolling process, the control system of the cold continuous rolling mill set adjusts and controls the emulsion concentration of each stand respectively according to the optimal emulsion concentration set value obtained in the step (n).

To sum up, the technical solution of the invention changes the mode in the prior art that the emulsion in each stand adopts constant concentration control, takes the concentration of the emulsion in each stand as a variable to be optimized, and carries out comprehensive optimization control on the emulsion concentration, thus achieving suppressing the vibration of the rolling mill.

The method of the invention can be widely used in the field of controlling emulsion concentration of the cold continuous rolling mill set.

Claims

1. A method of emulsion concentration optimization for a cold continuous rolling mill set, comprising the following steps: (a) acquiring apparatus characteristic parameters of a cold continuous rolling mill set;(b) acquiring critical rolling process parameters of a strip material;(c) acquiring process parameters involved in the process of emulsion concentration optimization;(d) setting an initial set value of an emulsion concentration comprehensive optimization target function for a cold continuous rolling mill set for achieving vibration suppression: F0=1.0×1010;the executing order of steps (a) to (d) is not limited;(e) calculating a bite angle α, of each stand;(f) calculating a vibration determination index reference value ξ0i of each stand;(g) setting an emulsion concentration Ci of each stand;(h) calculating the outlet temperature Ti of a strip steel of each stand;(i) calculating the dynamic viscosity η0i of an emulsion in a roll gap of each stand;(j) calculating an oil film thickness ξi in the roll gap of each stand;(k) calculating the emulsion concentration comprehensive optimization target function F(X);(l) determining whether the inequation F(X)<F0 is established, if yes, then setting Ciy=Ci, F0=F(X) and turning to step (m); if no, directly turning to step (m);(m) determining whether the emulsion concentration Ci exceeds the range of a feasible region, if yes, turning to step (n); if no, turning to step (g), wherein the feasible region refers to a region from 0 to the maximum emulsion concentration allowed by an apparatus;(n) outputting the optimal emulsion concentration set value Ciy, wherein Ciy is the value of Ci when the calculated value of F(X) is minimum in the feasible region; and(o) adjusting and controlling the emulsion concentration of each stand according to the optimal emulsion concentration set value Ciy in the step (n) by a control system of the cold continuous rolling mill set; andin each formula, i represents the stand ordinal number of the cold continuous rolling mill set.

2. The method of claim 1, wherein calculating the vibration determination index reference value ξ0i of each stand in the step (f) comprising the following steps: (f1) calculating an over-lubricated oil film thickness critical value ξi+ of each stand as follows:

3. The method of claim 1, wherein calculating the outlet temperature Ti of the strip steel of each stand in the step (h) comprising the following steps: (h1) calculating the outlet temperature Ti of the first stand:

4. The method of claim 1, wherein the apparatus characteristic parameters of the cold continuous rolling mill set at least comprise: the radius Ri of a work roll of each stand; the surface linear speed vri of a roll of each stand; the original roughness Rair0 of a work roll of each stand; the roughness attenuation coefficient BL of a work roll; the distance l between stands; and rolling kilometers Li of a work roll of each stand after roll change; wherein i=1, 2, . . . , n; i represents the ordinal number of the stand of the cold continuous rolling mill set, and n is the total number of the stands.

5. The method of emulsion concentration optimization for the cold continuous rolling mill set as claimed in claim 1, wherein the critical rolling process parameters of the strip material at least comprise: the inlet thickness H0i of each stand; the outlet thickness h1i of each stand; the width B of the strip steel; the inlet speed v0i of each stand; the outlet speed v1i of each stand; the inlet temperature T1Inlet; the resistance to deformation Ki of the strip steel of each stand; the rolling pressure Pi of each stand; the back tension T0i of each stand; the front tension T1i of each stand; the concentration influence coefficient kc of the emulsion; the viscosity compression coefficient θ of a lubricant; the density ρ of the strip steel; the specific heat capacity S of the strip steel; the flow rate w of the emulsion; the temperature Tc of the emulsion; and the mechanical equivalent of heat J.

6. The method of claim 1, wherein the process parameters involved in the process of emulsion concentration optimization at least comprise: the over-lubricated oil film thickness critical value ξi+ and the corresponding friction coefficient ui+ of each stand; the under-lubricated oil film thickness critical value ξi− and the corresponding friction coefficient ui− of each stand; and the vibration determination index reference value ξ0i; the rolling reduction Δhi=h0i−h1i; the rolling reduction ratio

7. The method of claim 1, wherein the calculation formula for calculating the bite angle αi of each stand is as follows:

8. The method of claim 1, wherein the calculation formula for calculating the dynamic viscosity η0i of the emulsion in the roll gap of each stand is as follows: η0i=b·exp(−a·Ti)wherein a and b are dynamic viscosity parameters of the lubricant under atmospheric pressure.

9. The method of claim 1, wherein the calculation formula for calculating the oil film thickness in the roll gap of each stand is as follows:

10. The method of in claim 1, wherein the emulsion concentration comprehensive optimization target function is calculated according to the following formula: