dc.description.abstract |
Exploration of Geothermal power has gained momentum in the recent past as it has
proved dependable, has reduced green gas emissions, met diversification needs,
provides least cost base load mode of power generation and is inexhaustible for billions
of years to come. However, the development and exploitation of geothermal resource
face a notable challenge of scale formation on the steam lines and most surface
equipment, leading to reduced and expensive production. Scaling occur mainly due to
deposition of solids carried by steam. One of the important scale solubility factor is the
pH of the brine. Low pH levels are associated with Non Condensable Gases (NCGs)
carryover which enhances scaling. Reduced production due to scaling is demonstrated.
For example, it was established from Olkaria production logs that from Nov 2018-Feb
2019, when the unit was experiencing scaling, KenGen lost a total of 7,825,685KWh
translating to US$ 688,660.28, considering electricity sale price as 0.008 US$/ Kwh due
to scaling. The recent used strategies like use of Organic Rankine Cycle (ORC) bottoming
plant to the existing facility for initially designed geothermal systems, use of combined
cycle plants and pH mod has led to reduced scaling and additional production. ORC
involves use of heat exchanger and a secondary working fluid to drive turbines. pH mod
involves online monitoring and control of silica in the reinjection pipelines using a
chemical process treatment equipment. Combined cycle technology involves use of a
steam turbine and ORC technology in one plant. ORC is not typically cost effective
especially for modular wellhead plant while pH mod considers only scaling in
reinjection pipelines. This means that scaling challenge is still at large especially for
initially installed single flush geothermal stations like Olkaria II leading to losses of large
amount of energy.
This study explored the design and implementation of a real time scale level monitoring
and control for geothermal energy generation system based on a physical T5554 analytic
process control system. A virtual system was designed using Siemens NX and
programmed using Totally Integrated Automation (TIA) software, PORTAL V14 via
Programmable Logic Controller -1200 PLC, CPU 1214C DC/DC/DC 6ES7 214-1AG40-
OXBO hardware. A set point pH of 6.5, an appropriate point to prevent scaling, as
guided by the practice in Olkaria II was used with the PID of the PLC to control the pH
of the analytic process control system. The virtual and the physical model were linked
to achieve communication through a channel called Open Platform Communication
(OPC) via KEP server, which is an interoperability standard for secure and reliable
exchange of data in industrial automation. Siemens NX design was configured to
communicate with KEP server via External Signal Configuration feature. This facilitated
the merger of control signals between Siemens NX design and TIA design. The TIA
portal used links that specified the sensor and actuator control signals. The system was
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4th Annual 1nternational Conference Innovative Technology for a Dynamic World 61
verified by pH readings of the two systems. The pH Data of the of the two systems
indicated a standard deviation of 8.25578E-4 before acidic condition correction by the
metering pump and a standard deviation of 0.01325 upon correction. The time lag was
so small that it did not affect the working of the system. This confirmed that the digital
model could be used to accurately represent the physical system and achieve scale
monitoring and real time control through managing the always changing brine pH in
geothermal fields. |
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