Abstract
The purpose of energy-saving improvement is not only to save energy but also to bring economic benefits, any energy-saving will contribute also to CO2 reduction. Generally, saving energy can reduce costs including saving Carbon Tax. Investment costs and energy-saving benefits are a pair of complementary contradictions; under specific conditions, to organically unify investment and benefits to produce maximum benefits is what we call optimization methods. This Chapter discussed the relationship between process rate and exergy loss, including heat transfer process, flow flowing process, mass transfer, and chemical reaction processes, especially discussed identifying the effectiveness of the driving force, proposed the driving force efficiency estimate method; following the optimization method, proposed the following process optimization approach and results: Economical insulation thickness of hot fluid pipeline; Economical pipe diameter and insulation thickness for fluid transportation, Optimization of heat exchange equipment; Economical thermal efficiency of the heating furnace.
Access this chapter
Tax calculation will be finalised at checkout
Purchases are for personal use only
References
Shanghai Institute of Chemical Engineering, Basic Chemical Engineering (Shanghai Science and Technology Press, 1978)
Tianjin University Chemical Engineering Principles Teaching and Research Office, Chemical Engineering Principles (Tianjin Science and Technology Press, 1983), pp. 78, 98
B. Hua, Process Energy Analysis and Synthesis (Hydrocarbon Processing Press, 1989), pp. 103–104
Y. Yang, Practical Chemical Systems Engineering (Chemical Industry Press, 1989)
S. Wei, Petrochemical Production Process Optimization (Refinery Design Editorial Department, 1988)
Y. Xu et al., Petrochemical Practical Optimization Method (Petroleum University Press, 1990)
H. Cao, K. Xie, Introduction to optimization methods. Refin. Des. 3 (1983)
X. Xiang, Engineering Exergy Analysis Method (Petroleum Industry Press, 1990), pp. 312–317
R.A. Gaggioli, Second Law Analysis for Process and Energy Engineering (American Chemical Society, 1983), pp. 34, 42
T.A. Chen, Economic pipe diameter and economic insulation thickness of fluid transport. Petrol. Refin. 10 (1986)
B. Lin et al., Economic Flow Velocity and Pipe Diameter of Oil Storage and Transportation. Oil Gas Storage Transp. 2 (1982)
S. Wei, Best heat exchanger area calculation method for a single heat exchanger. J. Beijing Chem. Inst. 1, 42, 51 (1981)
W. Li, Economic temperature difference of fired heater waste heat recovery. Petrol. Refin. 1 (1984)
Survey of the Technical Transformation of Refineries, Refinery Energy Conservation 10-Fired Heaters (Science and Technology Information Institute of the Ministry of Petroleum, 1985), pp. 67–71
S. Zhao, Q. Chen, Heating furnace heat efficiency technical and economic analysis. Refin. Des. 1 (1982)
D. Yang, Principles of Irreversible Process Thermodynamics and Engineering Applications (Science Press,1989), p. 2
B. Hua, A. Chen, Practical calculation and exergy economic analysis of heat dissipation in refinery. Petrol. Refin. 2 (1984)
W.J. Weper et al., Economics Sizing of Steam Piping and Insulation (1980)
Author information
Authors and Affiliations
Corresponding author
Rights and permissions
Copyright information
© 2022 The Author(s), under exclusive license to Springer Nature Singapore Pte Ltd.
About this chapter
Cite this chapter
Chen, T.A. (2022). Optimization on Pipeline and Equipment. In: Energy Saving and Carbon Reduction . Springer, Singapore. https://doi.org/10.1007/978-981-19-5295-1_12
Download citation
DOI: https://doi.org/10.1007/978-981-19-5295-1_12
Published:
Publisher Name: Springer, Singapore
Print ISBN: 978-981-19-5294-4
Online ISBN: 978-981-19-5295-1
eBook Packages: EnergyEnergy (R0)