LINDSEY OIL REFINERY LIMITED, UK UTILITIES INTEGRATED MONITORING AND CONTROL SYSTEM

Introduction

The goal of this project was to develop and build this system in order to integrate the control of the electric utility with the other production islands control of the refinery. As a result, the following achievements were sought after:

- Increase of the reliability;
- Increase of the efficiency;
- Electric Power Consumption and Production expenditures optimization;
- Electricity Quality improvement, in regard to internal and National Grid requirements;
- Increase of the efficiency of the operators actions;
- Maximum efficient follow up of the operative personnel;
- Maximum operative personnel protection and improper operator actions effect minimizing;
- Process and personnel actions follow up data base consolidation in order to achieve integrated solution of the tasks of the Electric Utilities Management, including online assessment of the equipment residual recourses and flexible maintenance planning. The last function was planned to be implemented in the near future.

Background

The electrical network at Lindsey Oil Refinery was operated and monitored from two main hardwired panels located within the Utilities Control Room:
- ‘AEI’ Panel
- ‘CHP’ Panel.

The AEI panel was over thirty years old and mainly comprised control and current monitoring of 11kV and 415V circuit breakers within the Utilities Substation. It also provided:

- Manual synchronization of generators 8G-1&2;
- Power measurements ;
- Alarm handling;
- Speed governor control;
- Voltage regulator control;
- Disturbance recording.

The CHP panel was more modern and performed similar duties to the AEI panel, but handling one 40MW gas turbine generator (9G-1) and monitored and controled upstream Yorkshire Electricity & Inoggy supplies to the LOR electrical network.

Hardwired contacts at the CHP panel, initialized automatic plant wide load shedding. Current monitoring at the AEI panel allowed selective plant load shedding to take place.

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THE TASKS, THE FULFILLEMENT OF WHICH IT ENABLED THE GOAL TO BE ACHIEVED

- To transfer existing electrical control functions from the Utilities Control Room to a Centralized Control Room by means of the objectives:

- To provide facilities to monitor and control electrical plant remotely from a central location.
- To allow the plant to overcome the problems and constraints associated with thirty-year-old technology and equipment;
- To take advantage of current technology in providing the required flexibility and reliability for the new system to be easily modified, developed and integrated with other plant systems;
- To simplify the existing relay panels by deriving control from microprocessor based equipment and overcoming maintenance problems associated with aging relay logic;
- The contain high capacity for future development and expansion and the ability to interrogate for errors and provide effective man machine interface. The system will also provide increased ease for faultfinding and reduced breakdown time.


FEATURES SPECIFICATION

Introduction

The system’s basic functions are:
- Provision of a ‘soft’ control system to monitor and control the main 11,000 volt electrical network;
- Provide automatic and manual control and synchronization of existing 11kV generators 8G-1 and 8G-2;
- Interface with the electrical power system via dedicated transducers for system analysis and trending.;
- Replicate the existing CHP system hardwired controls to screen based mimics. Interface with the existing Burner Management System panel;
- Control and monitoring of 3.3kV and 415V Utilities switchboards;
- Monitor the Central Control Room building internal distribution equipment;
- Implement optimized load shedding at emergency situations;
- Interface with the existing Plant Steam Production Control Subsystem;


System overview

The low layer of the system is based on two triple modular redundant TRICON 9.6 controllers. The control function is distributed on the principle, which allows the system to remain “alive” if one of the controllers completely fails. Such failure practically is impossible due to the fact that the controllers have very high availability , because of their triple redundancy. Field records of 250 years MTBF are available.

Supply Power Quality Monitoring

General requirements for switchboards 1A, 2B, 3A and 4B are to analyze the Power Quality of the system in terms of disturbances, i.e. the system provides information on:

· Supply interruptions
· Voltage sag & swell
· Harmonics
· Transients
· Noise
· Poor power factor
· Crest factor

Waveforms are displayed on a dedicated mimic page selected by the operator.

Synchronisation

Synchronisation is automatic and manual. The two 11kV generators 8G-1 and 8G-2are treated as individual units with hardware and software design reflecting this philosophy.
The synchronization function was raised as one of the most important , because it has to be done frequently. The reason of that was the demand for the Refinery Electric Power System to be flexible and efficient.

Generating from the controllers correction signals to the voltage and speed is the synchronization procedure, done by regulating system of the power supply being synchronized.
The permissive for this procedure to start is the availability of a set of parameters.
The check of availability if these parameters is done by means of software and hardware redundancy.
If some signals are missing the procedure starts again. After three unsuccessful attempts, the system generates alarm signal.

High accuracy of synchronization was achieved, which brings high quality and long life of the equipment. Low qualified personnel can initiate this procedure.

Six synchronizing references will be necessary to fulfill total system synchronization. These are shown on the attached sketch URS_FIG02 and listed below:

1) LOR Incomer 1
2) Bus Bars 1A
3) Generator 8G-1
4) LOR Incomer 2
5) Bus Bar 2B
6) Generator 8G-2

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Operation following Synchronization

Background

Turbo-generators 8G-1 and 8G-2 have two modes of control; Speed control and Back Pressure Control. On speed control the objective is to maintain a constant MW output from the generators. This results in a constant low pressure steam flow from the turbine driver outlet into the refinery low pressure steam main header, giving a varying pressure in the low pressure steam main, depending on demand.
On Back Pressure Control, the objective is to maintain a constant pressure on the refinery low-pressure steam main header. This results in a varying MW output from the generators, as the turbine governor automatically adjusts in order to maintain the refinery low pressure steam header pressure. Thus in this mode, the electrical power generated varies in direct proportion to the low-pressure steam demand of the refinery.
The low pressure steam system can vary considerably depending on process demand, therefore normal operating mode for the Turbo- generators is on Back Pressure Control to maintain a constant pressure on the low pressure steam system.

“Back Pressure Control” Mode.

This mode is only possible when the frequency is being held constant by a second generator (9G-1) or when running parallel with the National Grid.

When operating in Back Pressure Control, an increase in the back pressure will be corrected via the pressure set point change to the Controller, which will cause the inlet valves to close accordingly.
Control can also be set at negative values, e.g. it is possible to compensate for pressure loss ( process demand for steam ).

If the National Grid Supply were lost the turbine generators would automatically change over to speed control . The speed control device will be pre-set at its upper limit , therefore the generators output would increase to maximum ,this in turn will reduce the amount of electrical load shedding required and ensure stable frequency control.
Any change over of turbine controls will be bump-less to ensure the stability of the refinery electrical and steam systems.

LOAD SHEDDING

Load shedding package provides for different scenarios, in regard with the specific situation. This results to increasing the refinery flexibility to keep the processes running to the maximum possible extent. The Load Control is implemented with high reliability by means of the triple redundant controllers and the hot backed up Supervisory control via the both Workstations.

NEW MNEMONIC SCREENS

New mnemonic panels were in the scope of the supply. They were built on a modern contemporary style. Along with the live light indication, digital presentation of selected parameters was provided.

The control priority via these panels was arranged through a specific priority.

Communication to the Steam producing Sub-system

A communication was established between the two systems, realizing bilateral data flow, which resulted to overall control backup.

Energy Metering and electric power import-export optimization

Special software shell over the turbo-generator control algorithms was developed. This shell ensures import/export energy measuring, as well as, power factor or reactive power control.
The continuous import/export consumed and produced energy improved the utility efficiency.

Supervisor Monitoring and Control through the Main Control Room

Function of monitoring of the Main Control Room Power Supply and its active backing up through Uninterruptible Power Supply and Diesel generator was added to the System.

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Reference for this product

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