The Modified Configuration of Wet Wash System in the Gulf of Thailand

2021 ◽  
Author(s):  
Khemchad Sumitra ◽  
Marty Fernau ◽  
Karn Thanomkiat ◽  
Joseph Ritcey ◽  
Chadchai Tumtong

Abstract "Wet Wash" is a concept whereby cuttings are fluidized then sent to centrifuges to seperate the fluids from the cuttings. A modified configuration of this Wet Wash system improves fluids performance while minimizing environmental impact and optimizing operating costs. The original Wet Wash system, introduced in 2006, started at the shale shakers where big cuttings were removed by the scalping deck and diverted overboard. Only the small cuttings from the primary deck were fluidized and transported to a big bowl centrifuge. For the original system, the % Synthetic on Cuttings (SOC) for this process was always over 8.0%. The system was unable to lower the SOC due to concerns for the capability of the big bowl centrifuge to handle big cuttings. With a modified centrifuge unit, a more robust unit with a design change in feed nozzles being able to handle more torque, all cuttings from both scalping deck and primary deck are fluidized and transported to a big bowl centrifuge with no big cuttings diverted overboard. Utilizing the previous configuration of Wet Wash whereby cuttings from the scalper deck were diverted overboard, the % SOC was always over 8.0%. It was efficient in the removal of solids, but it was still yielding high SOC. In 2012 the use of Cuttings Dryers was introduced to further reduce % SOC. On Jack-up rigs, the Cuttings Dryer can operate in a normal manner, but on Tender Assisted rigs, where the cuttings are fluidized and pumped to the Dryer, there is a trade-off. High content of Low Gravity Solids (LGS) from the continual grinding of the solids to ultrafine particles that could not be removed by centrifuges had become an issue. High dilution rates were required to keep mud system under control due to excessive ultrafine solids. The Wet Wash system was re-visited for Tender Assisted rigs. With the modified configuration of Wet Wash system where no cuttings were diverted overboard, fluids performance was improved from reduction of ultrafine solids contamination in the mud system, resulting in less dilution rate and mud chemicals treatment. The % SOC was also lower than 8.0%. With proper Preventative Maintenance (PM) program in place, there was neither down time of the centrifuge nor report of excessive wear of equipment from handling big cuttings. The novelty of the modified Wet Wash configuration is in the ability to improve fluids performance and reduce environmental impact with the optimum operating cost.

2017 ◽  
Vol 2017 ◽  
pp. 1-10 ◽  
Author(s):  
Xiao Chai ◽  
Xiongqing Yu ◽  
Yu Wang

To investigate more efficient aircraft configurations which have less environmental impact, this paper develops a multidisciplinary analysis framework integrated with the airframe and propulsion analysis modules. The characteristics for propulsion, aerodynamics, weight, performance, cost, emissions, and noise can be rapidly predicted by the framework. The impact of propulsion installation with large diameter engines on aircraft weight and drag are considered in the framework. A wide-body aircraft was taken as an example for the optimization to investigate the tradeoffs between the cost metric and the environmental performance metrics. Several cases for single objective and multiobjective optimizations were performed. In the single objective optimizations, the direct operating cost, the cumulative noise, the oxides of nitrogen emissions during landing-takeoff cycle, and the mission oxides of nitrogen emissions were considered as an objective and minimized, respectively. The different objectives resulted in designs with different airframe parameters and engine cycle parameters. In the multiobjective optimizations, the direct operating costs and environmental performances were considered as the objectives simultaneously. The optimization results were the Pareto fronts for the minimum direct operating costs and environmental performances, which illustrate the quantitative relationships between the economic metric and the environmental performances.


2021 ◽  
Vol 13 (4) ◽  
pp. 168781402110106
Author(s):  
John Rios ◽  
Rodrigo Linfati ◽  
Daniel Morillo-Torres ◽  
Iván Derpich ◽  
Gustavo Gatica

An efficient distribution center (DC) is one that receives, stores, picks and packs products into new logistics units and then dispatches them to points of sale at the minimal operating cost. The picking and packing processes represent the highest operating cost of a DC, and both require a suitable space for their operation. An effective coordination between these zones prevents bottlenecks and has a direct impact on the DC’s operational results. In the existing literature, there are no studies that optimize the distribution of the picking and packing areas simultaneously while also reducing operating costs. This article proposes an integer nonlinear integer programming model that minimizes order preparation costs. It does so by predicting customer demand based on historical data and defining the ideal area for picking and packing activities. The model is validated through a real case study of seven clients and fifteen products. It achieves a [Formula: see text] reduction in operating costs when the optimal allocation of the picking and packing areas is made.


2004 ◽  
Vol 50 (7) ◽  
pp. 243-248 ◽  
Author(s):  
J. Clauson-Kaas ◽  
T. Sander Poulsen ◽  
B. Neergaard-Jacobsen ◽  
T. Guildal ◽  
C. Thirsing

Do operating costs conform to environmental impact after introduction of charges on discharge of wastewater? A study on optimization of phosphorus removal at two Danish wastewater removal plants shows that this is actually the case. By measurement of inlet and outlet concentrations and of chemicals added it was possible to determine the relationships between chemical dosing and phosphorus discharge and thus calculate the operational cost and environmental impact of different dosing/discharge levels.


2015 ◽  
Vol 71 (9) ◽  
pp. 1286-1292 ◽  
Author(s):  
Steen Nielsen

The effect on the environment of the establishment and operation of a sludge treatment reed bed system (STRB) is quite limited compared to mechanical sludge dewatering, with its accompanying use of energy and chemicals. The assessment presented here of the investment, operation and maintenance costs of a typical STRB, and of the related environmental impact, is based on the experiences gained from the operation of a large number of STRB in Denmark. There are differences in the environmental perspectives and costs involved in mechanical sludge dewatering and disposal on agricultural land compared to STRB. The two treatment methods were considered for comparison based on a treatment capacity of 550 tons of dry solids per year and with land application of the biosolids in Denmark. The initial capital cost for STRB is higher than a conventional mechanical system; however, an STRB would provide significant power and operating-cost savings, with a significant saving in the overall cost of the plant over 20–30 years. The assessment focuses on the use of chemicals, energy and greenhouse gas emissions and includes emptying, sludge residue quality and recycling. STRB with direct land application is the most cost-effective scenario and has the lowest environmental impact. A sludge strategy consisting of an STRB will be approximately DKK 536,894–647,636 cheaper per year than the option consisting of a new screw press or decanter.


1986 ◽  
Vol 10 (1) ◽  
pp. 10-15 ◽  
Author(s):  
Dennis A. Werblow ◽  
Frederick W. Cubbage

Abstract Forest harvesting equipment purchase costs in 1984 were determined by a survey of equipment dealers and manufacturers operating in the South. Based on delivered purchase prices, fixed costs for equipment ownership were calculated using machine rate formulas. Equipment operating costs were estimated based on general guidelines, fuel consumption data, and historical records. The fixed and operating cost data can be used when considering equipment investments and analyzing actual or potential harvesting systems.


2015 ◽  
Vol 45 (9) ◽  
pp. 1713-1719 ◽  
Author(s):  
Gerson de Freitas Silva Valente ◽  
Regina Célia Santos Mendonça ◽  
José Antônio Marques Pereira

<p>This research deals with the investigation of electrocoagulation (EC) treatment of wastewater from a dairy plant using aluminum electrodes. Electrolysis time, pH, current density and distance between electrodes were considered to assess the removal efficiency of chemical oxygen demand (COD), total solids (TS) and their fractions and turbidity. Samples were collected from the effluent of a dairy plant using a sampling methodology proportional to the flow. The treatments were applied according to design factorial of half fraction with two levels of treatments and 3 repetitions at the central point. The optimization of parameters for treating dairy industry effluent by electrocoagulation using aluminum electrodes showed that electric current application for 21 minutes, an initial sample pH near 5.0 and a current density of 61.6A m<sup>-2</sup> resulted in a significant reduction in COD by 57%; removal of turbidity by 99%, removal of total suspended solids by 92% and volatile suspended solids by 97%; and a final treated effluent pH of approximately 10. Optimum operating condition was used for cost calculations show that operating cost is approximately 3.48R$ m<sup>-3</sup>.</p>


2020 ◽  
Vol 9 (4) ◽  
pp. 174
Author(s):  
Youhong Liu

At present, the medical industry has developed into a sunrise industry in the new era. With the continuous improvement of the level of medical services and technical requirements and the establishment and improvement of related medical service institutions, the competition between the medical industries is further intensified. As a complex, hospitals must achieve cost control and financial management in order to achieve ideal operating benefits. At present, there are still many problems in the financial management and cost control of related hospitals. For this, it is necessary to grasp the problem and take effective measures to cope with it, promoting the effective control of hospital operating costs, and achieving efficient financial management goals.


Author(s):  
Erin E Powell ◽  
Gordon A Hill

The operation of continuously stirred tank bioreactors (CSTBs) at minimum cost is a major concern of operators. In this work, a CSTB design strategy is presented where impeller stirring speed and aeration rate are optimized to meet the oxygen demand of growing cells, simultaneously minimizing the capital and operating cost. The operating cost is limited to the cost of utilities. The optimization scheme assumes a given fermentor tank size, and that the properties of the culture medium and the oxygen respiratory requirements of the microorganisms being cultivated are known. It is possible to choose between two different turbine impellers during the design process. The equations, constraints, and the CSTB design strategy employed by the program are described. The effect of microbial species, ions in the culture medium, impeller style, as well as changing CSTB size and biomass input density on the optimum operating conditions, is examined. The mass transfer coefficient, gas holdup, mixing speed, and aeration rate are all reported at optimized cost conditions. A study of the effects of various parameters on the CSTB design are shown.


Author(s):  
Alta Knizley ◽  
Pedro J. Mago

This paper evaluates the economic, energetic, and environmental feasibility of using two power generation units (PGUs) to operate a combined heat and power (CHP) system. A benchmark building developed by the Department of Energy for a full-service restaurant in Chicago, IL is used to analyze the proposed configuration. This location is selected since it usually provides favorable CHP system conditions in terms of cost and emissions reduction. In this investigation, one PGU is operated at base load to satisfy part of the electricity building requirements (PGU1), while the other is used to satisfy the remaining electricity requirement operating following the electric load (PGU2). The dual-PGU configuration (D-CHP) is modeled for several different scenarios in order to determine the optimum operating range for the selected benchmark building. The dual-PGU scenario is compared with the reference building using conventional technology to determine the economical, energetic, and environmental benefits of this proposed system. This condition is also compared to a CHP system operating following the electric load (FEL) and to a base-loaded CHP system, and it provides greater savings in operating cost, primary energy consumption, and carbon dioxide emissions than the optimized conditions for base loading and FEL.


2020 ◽  
Vol 44 ◽  
Author(s):  
Nilton Cesar Fiedler ◽  
Alexandre Arantes de Campos ◽  
Marcos Vinicius Winckler Caldeira ◽  
Julião Soares de Souza Lima ◽  
Antônio Henrique Cordeiro Ramalho ◽  
...  

ABSTRACT Mechanization in forestry implantation demands high energy, time, and high operational and production costs. Thus, studies related to the influence of variables on the efficiency of these activities are essential to reduce costs and optimize operations. The objective of this study was to evaluate the operational and cost performance of mechanized forest implantation operations in Eucalyptus sp. Data were collected from eucalyptus plantations located in the northern region of the state of Espírito Santo, Brazil. The analysis of operational performance determined the distribution of operating times, mechanical availability, degree of utilization, operational efficiency, and productivity of the machines. The cost analysis estimated the operating costs in forestry implantation activities. The forest planting operations were: waste removal, subsoiling, digging with fertilization, planting, chemical weeding, and covering fertilization. According to the results, planting (39.20%) and waste removal (15.99%) represented the longest operating cycle times, the shortest production times (51.48% and 53.64%), and finally the longest maintenance times (32.95% and 29%). Chemical weeding and subsoiling showed the lowest maintenance times (4.64% and 3.47%). The cover fertilization was the operation that presented the highest productivity (2.99 ha he-1), and the removal of residues had the lowest (0.97 ha he-1). The highest costs per effective hour (R$13.57 he-1) and lowest production costs (R$81.59 ha-1) occurred at planting. Subsoiling had the highest production cost (R$112.80 ha-1). The lowest operating cost was obtained in the fertilizing operation. Operating costs had the greatest weight in labor, fuel, and maintenance and repairs.


Sign in / Sign up

Export Citation Format

Share Document