scholarly journals Heat integration and operational optimization of an austenitization furnace using concentric‐tube radiant recuperators

AIChE Journal ◽  
2018 ◽  
Vol 65 (7) ◽  
pp. e16414 ◽  
Author(s):  
Hari S. Ganesh ◽  
Ofodike A. Ezekoye ◽  
Thomas F. Edgar ◽  
Michael Baldea
Keyword(s):  
Heat Integration ◽  
Operational Optimization

scholarly journals Operational optimization of a building-level integrated energy system considering additional potential benefits of energy storage

2021 ◽  
Vol 6 (1) ◽  
Author(s):  
Sai Liu ◽  
Cheng Zhou ◽  
Haomin Guo ◽  
Qingxin Shi ◽  
Tiancheng E. Song ◽  
...  
Keyword(s):  
Energy Storage ◽  
Operating Cost ◽  
Economic Cost ◽  
Energy System ◽  
Peak Shaving ◽  
Operational Optimization ◽  
Integrated Energy System ◽  
Potential Benefits ◽  
The Times ◽  
Building Level

AbstractAs a key component of an integrated energy system (IES), energy storage can effectively alleviate the problem of the times between energy production and consumption. Exploiting the benefits of energy storage can improve the competitiveness of multi-energy systems. This paper proposes a method for day-ahead operation optimization of a building-level integrated energy system (BIES) considering additional potential benefits of energy storage. Based on the characteristics of peak-shaving and valley-filling of energy storage, and further consideration of the changes in the system’s load and real-time electricity price, a model of additional potential benefits of energy storage is developed. Aiming at the lowest total operating cost, a bi-level optimal operational model for day-ahead operation of BIES is developed. A case analysis of different dispatch strategies verifies that the addition of the proposed battery scheduling strategy improves economic operation. The results demonstrate that the model can exploit energy storage’s potential, further optimize the power output of BIES and reduce the economic cost.

Simultaneous process parameters and heat integration optimization for industrial organosilicon production

2021 ◽  
Vol 265 ◽  
pp. 118520
Author(s):  
Lu Jin ◽  
Xiaodong Zhang ◽  
Chengtian Cui ◽  
Zhijun Xi ◽  
Jinsheng Sun
Keyword(s):  
Process Parameters ◽  
Heat Integration ◽  
Simultaneous Process

Dynamic Modeling of CATOFIN® Fixed-Bed Iso-Butane Dehydrogenation Reactor for Operational Optimization

2016 ◽  
Vol 14 (1) ◽  
pp. 491-515 ◽  
Author(s):  
Zeeshan Nawaz
Keyword(s):  
Coke Formation ◽  
Fixed Bed ◽  
Process Intensification ◽  
Operating Conditions ◽  
Catalytic Dehydrogenation ◽  
Heating Rates ◽  
Reactor Model ◽  
Fuel Gas ◽  
Bed Temperature ◽  
Operational Optimization

AbstractThe catalytic dehydrogenation of iso-butane to iso-butylene is an equilibrium limited endothermic reaction and requires high temperature. The catalyst deactivates quickly, due to deposition of carbonaceous species and countered by periodic regeneration. The reaction-engineering constraints are tied up with operation and/or technology design features. CATOFIN® is a sophisticated commercialized technology for propane/iso-butane dehydrogenation using multiple adiabatic fixed-bed reactors having Cr2O3/Al2O3 as catalyst, that undergo cyclic operations (~18–30m); dehydrogenation, regeneration, evacuation, purging and reduction. It is always a concern, how to maintain CATOFIN® reactor at an optimum production, while overcoming gradual decrease of heat in catalyst bed and deactivation. A homogeneous one-dimensional dynamic reactor model for a commercial CATOFIN® fixed-bed iso-butane dehydrogenation reactor is developed in an equation oriented (EO) platform Aspen Custom Modeler (ACM), for operational optimization and process intensification. Both reaction and regeneration steps were modeled and results were validated. The model predicts the dynamic behavior and demonstrates the extent of catalyst utilization with operating conditions and time, coke formation and removal, etc. The model computes optimum catalyst bed temperature profiles, feed rate, pre-heating, rates for reaction and regeneration, fuel gas requirement, optimum catalyst amount, overall cycle time optimization, and suggest best operational philosophy.

scholarly journals Design of a Low-cost CO2 Capture Process Based on Heat Integration Technology

2014 ◽  
Vol 61 ◽  
pp. 365-368 ◽  
Author(s):  
Chunfeng Song ◽  
Yasuki Kansha ◽  
Masanori Ishizuka ◽  
Qian Fu ◽  
Atsushi Tsutsumi
Keyword(s):  
Co2 Capture ◽  
Low Cost ◽  
Heat Integration ◽  
Capture Process ◽  
Integration Technology

Heat-integration retrofit study of a petroleum refinery

1991 ◽  
Vol 38 (4) ◽  
pp. 253-262 ◽  
Author(s):  
Salih Dinçer ◽  
İnci Şentarli
Keyword(s):  
Petroleum Refinery ◽  
Heat Integration
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