Abstract
Energy efficiency is considered an important indicator after the efficiency term is one framework of economic planning. The review results show that the gained energy is completely different in industries due to the production line, raw material, used fuel, system automation, application of thermodynamic rules, and energy recovery applications. The thermal parameters of the machining system are the main indicators to determine the system's efficiency. Dynamic behavior, effectiveness, and thermal capacity limitation are some parameters used for the optimization of machining energy efficiency. The temperature, pressure, flow rate, and other operating conditions as a function of time are the physical quantities to determine the dynamic behavior. The machining tools are intensive energy-consuming types of equipment and mostly consume electricity in manufacturing industries.
The general approach for cost-effective planning is to set a complete energy-efficient system. Mass, energy, and exergy analyses are the general bases for the efficiency consideration of heat generation. But the easiest and most expeditious energy recovery is observed in effective machining like micromechanical systems and hybrid systems, up to 20% of overall losses can be recovered. If the general usage of steam to produce electricity is considered, controlling the existing configuration will improve energy efficiency by applying quantitative optimization of the electricity usage. This quantity can be increased by an extra 20%. To optimize the entire cogeneration or trigeneration machining system, a holistic approach is needed that improves the system's energy efficiency by up to 65%. The energy efficiency is increased in the range from 3 to 35% by innovative EMS. Air leaks are causing the highest energy losses in CA systems. More than 90% energy efficiency can be achieved with an appropriate CAES system mostly in isothermal and high-pressure conditions for machining purposes. Moreover, the recovered energy will mitigate GHGs. And it is strict that, any developing plan of countries which contains an energy efficiency strategy, is necessary to sustain a habitable earth.
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Data availability
The data presented in this study are available on request from the corresponding author.
Abbreviations
- cp-g :
-
Exhaust gas average specific heat
- Ebiomass :
-
Biomass input
- Ecoal :
-
Coal input
- Ecooling :
-
Cooling output
- Eheating :
-
Heating output
- Ei :
-
Total electricity demand (annual) (GJ/yr)
- Ein,i :
-
Exergy input to a component (kW)
- Eout,k :
-
Exergy output to a component (kW)
- ESy :
-
Electricity savings (measure y for x) (GJ/yr)
- EX :
-
Exergy (J)
- Exbiomass :
-
Exergies of biomass (kW)
- EXC :
-
Exergy values for cooling
- Excoal :
-
Exergies of coal (kW)
- Excompair :
-
Exergy values for compressed air
- EXgt :
-
Exergy (the net power output of gas turbine)
- EXH :
-
Exergy values for heating (kW)
- EXhot water :
-
Output exergy of the hot water (kW)
- EXin :
-
Input exergy of the system (kW)
- Exsewage :
-
Exergies of sewage (kW)
- EXst :
-
Exergy of power output of steam turbine (kW)
- Fy :
-
Fuel thermal content (kWh)
- H:
-
Hot
- h:
-
Enthalpy (specific) (kJ/kg)
- h1 :
-
Enthalpy of compressed air (kJ/kg)
- h2s :
-
Isentropic enthalpy of compressed air (kJ/kg)
- hf :
-
Enthalpy of fuel (kJ/kg)
- in:
-
Inlet
- \(\dot{{\text{I}}}\) :
-
Irreversibility or exergy loss (kW)
- k:
-
Heat transfer coefficient (W/mK)
- L:
-
Thickness (m)
- mc :
-
Coal consumption rate (kg/s)
- mcoal :
-
Mass flow rates of coal (kg/s)
- msevage :
-
Mass flow rates of sevage (kg/s)
- mw :
-
Waste consumption rate (kg/s)
- \(\dot{{\text{m}}}\) :
-
Mass flow rate (kg/s)
- \({\dot{{\text{m}}}}_{{\text{f}}}\) :
-
Flow rate of the fuel (kg/s)
- \({\dot{{\text{m}}}}_{{\text{g}}}\) :
-
Exhaust gas mass flow rate (kg/s)
- n:
-
Number of modules
- out:
-
Outlet
- P:
-
Air pressure (Pa)
- PC :
-
Power consumption of compressor (kW)
- PE :
-
Available extra power for the CAES (MW)
- Pgt :
-
Gas turbine power (MW)
- Pin :
-
Input power (W)
- Pnet :
-
Net power output (W)
- Pout :
-
Power output (W)
- PP :
-
Power output of pneumatic energy (W)
- Pst :
-
Steam turbine power (MW)
- Ptot,net :
-
Net total power output (kW)
- Pw,net :
-
Net power output of the waste (kW)
- Q:
-
Heat load
- QC :
-
Cooling air output (W)
- Qc :
-
Energy input of the coal (kW)
- Qcompair :
-
Compressed air output (W)
- Qexh :
-
Exhaust heat from gas turbine (MW)
- Qgain :
-
Energy gain (W)
- QH :
-
Heating air output (W)
- Qp :
-
Primary energy (kW)
- Qsf :
-
Steam flow energy (kW)
- Qw :
-
Energy input of the waste (kW)
- \(\dot{\text{Q}}\) :
-
Heat transfer (kW)
- \({\dot{\text{Q}}}_{1}\) :
-
Heat addition (the steam per cycle) (kW)
- \({\dot{{\text{Q}}}}_{2}\) :
-
Heat rejection (the steam per cycle) (kW)
- \({\dot{{\text{Q}}}}_{{\text{b}}}\) :
-
Recovered thermal power (kW)
- \({\dot{{\text{Q}}}}_{{\text{L}}}\) :
-
Heat recovered by LPE
- \({\dot{{\text{Q}}}}_{{\text{loss}}}\) :
-
Sum of heat Losses (W)
- \({\dot{{\text{Q}}}}_{{\text{out}}}\) :
-
Sum of useful heat outputs (W)
- \({\dot{{\text{Q}}}}_{{\text{s}}\&{\text{w}}}\) :
-
Transferred heat to the steam and water (kW)
- \({\dot{{\text{Q}}}}_{{\text{tot}}}\) :
-
Heat losses sum & useful heat outputs (W)
- q:
-
Heat flux (W/m2)
- qc,net :
-
The coal net caloric values (kJ/kg)
- qcoal :
-
Lower caloric values of coal (kJ/kg)
- qsevage :
-
Lower caloric values of sevage (kJ/kg)
- qw,net :
-
The waste net caloric values (kJ/kg)
- Si :
-
Total value of the boiler losses (%)
- T:
-
Temperature in unit °C
- \(\dot{\text{U}}\) :
-
Heat loss increment due to the saved steam (kW)
- V:
-
Volume of air (m3)
- W:
-
Power production by the cogeneration (kW)
- \({\dot{\text{W}}}_{\text{c}}\) :
-
Compressor set total work (kW)
- We :
-
The expander produced output work (kW)
- Win,j :
-
Supplied work (kW)
- Wnet :
-
Net power output (kW)
- Wout,l :
-
Work output (kW)
- Wp :
-
Pump set total work (kW)
- X:
-
Faulty samples
- X*:
-
Normal samples
- \(\alpha \) :
-
Portion of electricity demand by industrial motors
- \({\upbeta }_{{\text{i}}}\) :
-
Portion of system x in total electricity
- \({\upgamma }_{{\text{x}}}\) :
-
Portion of total electricity demand by system x
- ∆Tlift :
-
Temperature lift (°C)
- \({\upvarepsilon }_{{\text{c}}}\) :
-
Compression ratio
- \({\upeta }_{{\text{comp}}}\) :
-
Compressor efficiency
- \({\upeta }_{{\text{con}}}\) :
-
Conversion efficiency
- \({\upeta }_{{\text{el}}}\) :
-
Electrical efficiency
- \({\upeta }_{{\text{en}}}\) :
-
Energy efficiency
- \({\upeta }_{{\text{en}},{\text{tot}}}\) :
-
Total energy efficiency
- \({\upeta }_{{\text{en}},{\text{w}}}\) :
-
Waste-to-electricity efficiency
- \({\upeta }_{{\text{ex}}}\) :
-
Exergy efficiency
- \({\upeta }_{{\text{gt}}}\) :
-
Gas turbine efficiency
- \({\upeta }_{{\text{i}}}\) :
-
Standard efficiency
- \({\upeta }_{{\text{j}}}\) :
-
Increased efficiency
- \({\upeta }_{{\text{L}}}\) :
-
Low efficiency motor
- \({\upeta }_{{\text{Q}}}\) :
-
Thermal efficiency
- \({\upeta }_{{\text{RT}}}\) :
-
Round trip efficiency
- \({\upeta }_{{\text{s}}}\) :
-
Isentropic efficiency of the PM
- \({\upeta }_{{\text{st}}}\) :
-
Steam turbine efficiency
- \({\uptau }_{{\text{y}}}\) :
-
Share of total electricity demand by measure y
- ψ:
-
Specific exergy (kW/kg)
- A:
-
Area (m.2)
- B:
-
The replaced equipment age (years)
- C:
-
Cold
- D:
-
Lifetime of the equipment (years)
- d:
-
Adiabatic index
- CA:
-
Compressed air systems
- CAES:
-
Compressed air energy storage system
- CAP:
-
Chilled ammonia process
- CART:
-
Classification and regression tree
- CCHP:
-
Combined cooling, heating and power
- CFL:
-
Compact fluorescent light
- CFPP:
-
Coal-fired power plant
- CHP:
-
Combined heat and power
- CO2 :
-
Carbon dioxide
- COP:
-
Coefficient of performance
- CWSP:
-
Coal-water slurries containing petrochemicals
- DLFLN:
-
Double linear fast learning network
- EEM:
-
Energy efficiency measures
- EI:
-
Energy-relevant investment
- EMDS:
-
Electric motor driven systems
- EMR:
-
Energetic macroscopic representation
- EMS:
-
Electric motor systems
- EEM:
-
Energy efficiency measures:
- ERG:
-
Exhaust gas recirculation
- EUF:
-
Energy utilization factor
- FWH:
-
Feedwater heater
- GHGs:
-
Greenhouse gases
- GSHP:
-
Ground source heat pump
- HHV:
-
Higher heating value
- HTI:
-
Heat transfer intensification
- I-CAES:
-
Energy storage of isothermal compressed air
- IEE:
-
Improvement in energy efficiency
- LAES:
-
Liquid air energy storage
- LHV:
-
Lower heating value
- LPE:
-
Low-pressure economizer:
- MCHP:
-
Combined heat and power in micro sacle:
- MEA:
-
Monoethanolamine:
- NGCC:
-
Natural gas combined cycle
- NOx :
-
Nitrogen oxides
- NPV:
-
Net present value
- PM:
-
Pneumatic motor
- SO2 :
-
Sulfur dioxide
- TCO2ER:
-
Trigeneration CO2 emission reduction
- TDV:
-
Temperature driving force
- TI:
-
Total investment
- TRNSYS:
-
Transient System Simulation Tool
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A. Can: Conceptualization, Methodology, Validation, Formal Analysis, Investigation, Writing, Reviewing, Editing, Visualization, Supervision. N.H-OCAK: Writing—Original draft, Resources, Reviewing, Drawing.
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Ocak, N.H., Can, A. A review on energy efficiency techniques used in machining for combined generation units. Int J Interact Des Manuf (2024). https://doi.org/10.1007/s12008-024-01789-z
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DOI: https://doi.org/10.1007/s12008-024-01789-z