scholarly journals NGL Recovery Enhancement for GUPCO Trans Gulf Gas Plant by using New Applicable Technique

2019 ◽  
Vol 8 (3) ◽  
pp. 3723-3731

It is known that the price of natural gas liquids (NGL) is higher than that of natural gas from which it is derived, so more modifications needed for existing plants to derive more NGL is economically accepted point of view. The main objective of the present work is to present the method applied on Trans gulf (T/G) gas plant to overcome its performance decrease happened after the plant feed gases becoming leaner than its design margin and hence it led to a great decrease in the plant NGL recovery. This achieved by introducing a new simple modification to the existing process scheme obtained by using a condensate stream to enrich the reflux of the de-ethanizer tower so more recovery is obtained. In order to accomplish that goal, some changes in the existing process operating conditions were needed. A simulation is used in this study to examine the existing and the introduced modification utilizing ASPEN-HYSYS software version 8.4 using Peng-Robinson equation of state (EOS). The simulation of the existing plant results in a better understanding of the plant behavior in the different iterations to reach the maximum benefits. The plant after suffering from low butane recovery from its feed gas and which considered as a figure to the plant efficiency, it increased by this method from 38 % to reach 86-90 % butane recovery and its LPG production increased by 170% to be ≈ 122 tonne/day instead of ≈ 44 tonne/day while only losing ≈ 16 tonne/day of condensate production. An optimization to the new method is done in this paper so that it doesn't intercept with the existing plant equipment performance for the process safety triggers. Also, the last section of the study describes the economic point of view and the return on investment (ROI) how it was paid back only in 7 days. This modification can be taken as a guideline for both new and existing LPG plants which use only propane refrigeration systems for LPG recovery to increase their profits with the lowest cost possible.

Energies ◽  
2021 ◽  
Vol 14 (4) ◽  
pp. 1063
Author(s):  
Catalina Hernández Moris ◽  
Maria Teresa Cerda Guevara ◽  
Alois Salmon ◽  
Alvaro Lorca

The energy sector in Chile demands a significant increase in renewable energy sources in the near future, and concentrated solar power (CSP) technologies are becoming increasingly competitive as compared to natural gas plants. Motivated by this, this paper presents a comparison between solar technologies such as hybrid plants and natural gas-based thermal technologies, as both technologies share several characteristics that are comparable and beneficial for the power grid. This comparison is made from an economic point of view using the Levelized Cost of Energy (LCOE) metric and in terms of the systemic benefits related to flexibility, which is very much required due to the current decarbonization scenario of Chile’s energy matrix. The results show that the LCOE of the four hybrid plant models studied is lower than the LCOE of the gas plant. A solar hybrid plant configuration composed of a photovoltaic and solar tower plant (STP) with 13 h of storage and without generation restrictions has an LCOE 53 USD/MWh, while the natural gas technology evaluated with an 85% plant factor and a variable fuel cost of 2.0 USD/MMBtu has an LCOE of 86 USD/MWh. Thus, solar hybrid plants under a particular set of conditions are shown to be more cost-effective than their closest competitor for the Chilean grid while still providing significant dispatchability and flexibility.


Energies ◽  
2020 ◽  
Vol 13 (7) ◽  
pp. 1732 ◽  
Author(s):  
Muhammad Abdul Qyyum ◽  
Muhammad Yasin ◽  
Alam Nawaz ◽  
Tianbiao He ◽  
Wahid Ali ◽  
...  

Propane-Precooled Mixed Refrigerant (C3MR) and Single Mixed Refrigerant (SMR) processes are considered as optimal choices for onshore and offshore natural gas liquefaction, respectively. However, from thermodynamics point of view, these processes are still far away from their maximum achievable energy efficiency due to nonoptimal execution of the design variables. Therefore, Liquefied Natural Gas (LNG) production is considered as one of the energy-intensive cryogenic industries. In this context, this study examines a single-solution-based Vortex Search (VS) approach to find the optimal design variables corresponding to minimal energy consumption for LNG processes, i.e., C3MR and SMR. The LNG processes are simulated using Aspen Hysys and then linked with VS algorithm, which is coded in MATLAB. The results indicated that the SMR process is a potential process for offshore sites that can liquefy natural gas with 16.1% less energy consumption compared with the published base case. Whereas, for onshore LNG production, the energy consumption for the C3MR process is reduced up to 27.8% when compared with the previously published base case. The optimal designs of the SMR and C3MR processes are also found via distinctive well-established optimization approaches (i.e., genetic algorithm and particle swarm optimization) and their performance is compared with that of the VS methodology. The authors believe this work will greatly help the process engineers overcome the challenges relating to the energy efficiency of LNG industry, as well as other mixed refrigerant-based cryogenic processes.


2021 ◽  
Vol 2021 ◽  
pp. 1-10
Author(s):  
Lili Zuo ◽  
Sirui Zhao ◽  
Yaxin Ma ◽  
Fangmei Jiang ◽  
Yue Zu

During the process of distributing natural gas to urban users through city gate stations, hydrate is easy to form due to the existence of throttling effect which causes safety risks. To handle this problem, a program to quickly calculate hydrate prediction and prevention methods for city gate stations is developed. The hydrate formation temperature is calculated through the Chen–Guo model, and the Peng–Robinson equation of state combined with the balance criterion is used to analyze the water condensation in the throttling process. The Wilson activity coefficient model is used to calculate the mass fraction in the liquid phase of thermodynamic inhibitors for preventing hydrates. Considering the volatility of inhibitors, the principle of isothermal flash has been utilized to calculate the total injection volume of the inhibitor. Moreover, the effects of commonly used methanol and ethylene glycol inhibitors are discussed. In terms of safety and sustainability, the ethanol inhibitor, which is considered for the first time, exhibited better prevention and control effects under conditions with relatively high temperature and low pressure after throttling. Combined with the actual working conditions of a gate station, methanol has the best inhibitory effect, followed by ethylene glycol. From an economic point of view, the benefits of the gas phase of the inhibitor during the delivery of natural gas are obvious; therefore, the method of methanol injection is recommended for hydrate prevention. If the gas phase benefits of the inhibitor are not considered, the ethylene glycol injection method becomes more economical.


2021 ◽  
Vol 286 ◽  
pp. 02014
Author(s):  
Gheorghe Lăzăroiu ◽  
Lucian Mihăescu ◽  
Dana-Alexandra Ciupăgeanu ◽  
Rodica-Manuela Grigoriu ◽  
Dana-Andreya Bondrea

The paper presents an investigation on the conditions for implementing a methanation membrane decarbonator coupled to an energy installation that generates flue gases. The retention of the carbon dioxide content in the flue gases and its conversion to methane is envisaged. For start, low thermal power installations, employing natural gas as main fuel supply, are considered. Internal combustion engines (also working with natural gas fuel) are taken into account for the testing of the carbon dioxide retention process. For this, a classification of the flue gas composition by fuel categories is initially carried out. The decarbonation efficiency is defined and clarifications are made withal regarding the connection between the decarbonation installation and the energy plant. The first practical achievements are also presented, resulting from a decarbonator with a volume of 940 cm3 (having the inner diameter of 12 cm and a height of 50 cm). The results prove that the proposed solution has great potential for practical applications, further research being however necessary. In terms of operating costs (including hydrogen consumption), it is remarked that they can be reduced by exploiting the methane production and eliminating the carbon tax, extending the integration perspective form economic point of view.


2020 ◽  
Vol 12 (7) ◽  
pp. 1093
Author(s):  
Ignacio Martín Nieto ◽  
David Borge-Diez ◽  
Cristina Sáez Blázquez ◽  
Arturo Farfán Martín ◽  
Diego González-Aguilera

This research work aims at a multinational study in Europe of the emissions and energy costs generated by the operation of low enthalpy geothermal systems, with heat pumps fed by different energy sources. From an economic point of view, natural gas and biogas prices are, usually, lower than electricity ones. So it may be advantageous to use these energy sources to feed the heat pumps instead of electricity. From the environmental point of view, it is intended to highlight the fact that under certain conditions of electricity production (electricity mix), more CO2 emissions are produced by electricity consumption than using other a priori less “clean” energy sources such as natural gas. To establish the countries where each of the different heat pumps may be more cost-efficient and environmentally friendly, data from multi-source geospatial databases have been collected and analyzed. The results show that in the majority of cases, the electric heat pump is the most recommendable solution. However, there are some geographic locations (such as Poland and Estonia), where the gas engine heat pump may be a better alternative.


Author(s):  
Nesrin Ozalp

Among all fossil fuels, natural gas is probably the most attractive one because of its higher heating value, and approximately 97% methane content, which creates less hazardous emissions during power generation. Considering these important facts and the demand for natural gas in the world market, it would be unlikely to think of converting natural gas. However, if we want to utilize our planet’s limited natural gas resources better, then we need to explore alternative ways. A way to achieve that goal is direct cracking of natural gas via solar thermal processing. This paper describes advantages of solar cracking of natural gas from energy, environment and economic point of view. Results show that products of natural gas decomposition contain 8% more energy per mole compared to natural gas itself, while the decomposition process does not emit any hazardous emissions to the environment. As for the economics, once the decomposition products of natural gas, namely hydrogen and carbon black, are sold separately, it is possible to make up to three times more revenue than the selling of natural gas. The products of natural gas decomposition have a very wide use in chemical and petroleum industries. For example, hydrogen is a crucial commodity to refine crude oil, while carbon black is the fundamental component in car tire, battery, conveyer belt, and printer ink manufacturing industries. Currently, petroleum industry produces hydrogen via steam reforming of methane and the chemical industry produces carbon black from coal or natural gas combustion in furnace, which are both highly toxic and global warming emissive processes. With solar cracking of natural gas, these two important commodities can be produced without any emissions to the environment.


2018 ◽  
Vol 7 (1) ◽  
pp. 11-18
Author(s):  
Eric Farda

Water content in natural gas poses threat to process facilities such as column distillation. Natural gas from reservoirs usually contains water vapor, the presence of water vapor in gas processing causes bad impact to process facilities. Dry Gas composition data was taken from Salamander Energy. Optimization of natural gas dehydration using Tri Ethylene Glycol was carried out using Aspen HYSYS V8.6 with Peng-Robinson fluid package. The natural gas dehydrating plant was designed with operating conditions of 394 bar and 460C and 10 MMSCFD and 6.8 MMSCFD gas flow rate were inputted. Results obtained from HYSYS simulation shows. Three different TEG flowrates were used for this simulation. Results obtained from simulation that . For the purpose of running the plant economically, the minimum flow rate of TEG which will reduce the water content to within the limit of pipeline specification, is very important and the result obtained showed that a minimum of 3 m3/h of TEG is required to reduce the water content of a gas stream of 10MMSCFD to 6.8lb/MMSCFD, which is within the limit of 6-7lb/MMSCFD, this value when compare to gas plant which uses 15m3/h for the gas stream of 10MMSCFD to achieve the same water  content  specification is far lower.  Values below  this flow  rate  (3.5m3/h)  may not reduce the water content to the specified limit.


2016 ◽  
Vol 11 (3) ◽  
pp. 220-228
Author(s):  
Mariana Sarmanho de Oliveira Lima ◽  
Daisy Aparecida do Nascimento Rebelatto

2021 ◽  
Vol 136 (5) ◽  
pp. 19-22
Author(s):  
V. Ch. Ten ◽  
◽  
L. G. Lunkova ◽  
G. S. Melnikov ◽  
◽  
...  

The aim of the work is to study the energy efficiency of the «Arctic Cascade» technology used in the Russian project «Yamal-LNG». The company uses the reserves of the Yuzhno-Tambeyskoye field as a resource base. The relevance of the study is due to the imperfection of technological schemes in terms of the energy efficiency of liquefaction processes, as well as the lack of experience in operating LNG projects in Arctic conditions. This work presents the calculation of energy costs in the production of liquefied natural gas using the «Arctic cascade» technology using the example of the operating conditions of the Yamal-LNG plant, based on the model built in the Aspen Hysys. Modeling the technological scheme made it possible to apply the obtained data for the calculation, as a result of which the specific energy consumption of 230,78 kWh/t per ton of product was determined. It turned out that the technological solution has a significant drawback: a fairly high boil-off gas yield of 15.72% was revealed. This fact reduces the efficiency of the plant and leads to the need to re-feed it into the liquefaction cycle.


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