real-time process control
# Real-time Process Control
## Introduction & Motivation
Real-time process control through ML enables dynamic parameter adjustment and optimization during manufacturing operations.
Motivation: Achieve optimal control in real-time.
Applications: Adaptive control, feedback regulation, dynamic optimization, quality assurance.
---
## Core Concepts & Theory
### Feedback Control
Closed-loop regulation systems.
### Process Dynamics
Temporal response characteristics.
### Control Strategies
PID, MPC, and advanced methods.
### Optimization
Real-time parameter tuning.
---
## Mathematical Formulation
PID Control:
$$u(t) = K_p e(t) + K_i \int e(τ) dτ + K_d \frac{de}{dt}$$
Model Predictive Control:
$$u_t^* = \arg\min_u \sum_{i=1}^{H} ||y_{t+i} - y_{ref}||^2$$
Stability Criterion:
$$|G(jω)H(jω)| < 1$$
---
## Advanced Theory & Extensions
### Adaptive Control
Parameter adjustment algorithms.
### Nonlinear Control
Handling process nonlinearity.
### Robust Control
Uncertainty handling.
---
## Computational Considerations
Latency: O(1) processing.
Control: O(D²) network.
Throughput: High-frequency updates.
---
## Summary & Key Takeaways
ML enables real-time process control.
Principles: 1. Feedback, 2. Dynamics, 3. Stability, 4. Optimization, 5. Robustness.
---
## Appendix: Practical Labs
### Lab 1: PID Control Simulation
import numpy as np
class PIDController:
def __init__(self, Kp=1, Ki=0.1, Kd=0.1):
self.Kp = Kp
self.Ki = Ki
self.Kd = Kd
self.integral = 0
self.prev_error = 0
def control(self, error, dt):
self.integral += error * dt
derivative = (error - self.prev_error) / (dt + 1e-6)
u = self.Kp * error + self.Ki * self.integral + self.Kd * derivative
self.prev_error = error
return u
controller = PIDController()
for _ in range(10):
error = np.random.randn()
u = controller.control(error, 0.01)
assert isinstance(u, (float, np.ndarray)), "Control failed"
print(f"✓ PID control working")### Lab 2: Process Response
import numpy as np
def simulate_process(setpoint, control_input, process_gain=1.0):
"""Simulate first-order process"""
tau = 1.0
dt = 0.01
y = 0.0
dy = (process_gain * control_input - y) / tau
y += dy * dt
return y
setpoint = 100
for i in range(100):
u = 50
y = simulate_process(setpoint, u)
assert -500 < y < 500, "Process simulation failed"
print(f"✓ Process simulation working")### Lab 3: Control Loop
import numpy as np
def control_loop(setpoint, measurements, gains):
"""Execute control loop"""
Kp, Ki, Kd = gains
integral = 0
prev_error = 0
outputs = []
for y in measurements:
error = setpoint - y
integral += error
derivative = error - prev_error
u = Kp * error + Ki * integral + Kd * derivative
outputs.append(u)
prev_error = error
return np.array(outputs)
setpoint = 100
measurements = np.random.normal(100, 10, 50)
outputs = control_loop(setpoint, measurements, (1, 0.1, 0.1))
assert len(outputs) == 50, "Control loop failed"
print(f"✓ Control loop executed")### Lab 4: Stability Analysis
import numpy as np
def check_stability(gains, process_gain=1.0):
"""Check control stability"""
Kp, Ki, Kd = gains
gain_margin = 1 / (Kp * process_gain + 1e-6)
phase_margin = np.arctan(Kd / (Kp + 1e-6))
stable = gain_margin > 0.5 and phase_margin > 0.2
return stable
stable = check_stability((1, 0.1, 0.1))
assert isinstance(stable, (bool, np.bool_)), "Stability check failed"
print(f"✓ Stability: {stable}")---