DOMAIN-SPECIFIC LANGUAGE DEVELOPMENT FOR SMART CONTRACT SPECIFICATIONS

CO2 emissions have negative impacts on the environment, one of which is global warming. The cement production process accounts for 5% of global CO2 emissions. The increase in CO2 emissions from the cement production process continues. Carbon capture has potential to be the solution to reduce CO2...

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Main Author: Izzatur Rahman, Labib
Format: Theses
Language:Indonesia
Subjects:
Online Access:https://digilib.itb.ac.id/gdl/view/71717
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Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:71717
spelling id-itb.:717172023-02-21T14:42:54ZDOMAIN-SPECIFIC LANGUAGE DEVELOPMENT FOR SMART CONTRACT SPECIFICATIONS Izzatur Rahman, Labib Teknik (Rekayasa, enjinering dan kegiatan berkaitan) Indonesia Theses cement production, carbon dioxide, carbon capture, calcium looping, thermodynamic, Aspen Plus. INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/71717 CO2 emissions have negative impacts on the environment, one of which is global warming. The cement production process accounts for 5% of global CO2 emissions. The increase in CO2 emissions from the cement production process continues. Carbon capture has potential to be the solution to reduce CO2 emissions from cement factories. The carbon capture method that will be discussed in this final project is calcium looping. Calcium looping consists of two simple reactors consisting of a carbonator and calciner. Calcium looping material can be used as raw material for cement. The analysis was carried out by modeling and simulating the cement production process at Factory Pabrik V Indarung PT. Semen Indonesia. Simulations were carried out with Aspen Plus Ver. 11 software. The simulation of the application of calcium looping is carried out by adding carbonator and calciner components and making changes to the system as needed. The reduction in CO2 emissions after the calcium looping was applied is 37% for the coal fired system and 99% for the hydrogen fueled system. Fuel requirements increased by 94 kg/kg clinker for coal fired systems and 154 kg/kg clinker for hydrogen fueled systems. In addition, the increase in the ratio of the mole flow rate of CaCO3 added to the calcium looping to the mole flow rate of CO2 emissions (Fo/FCO2) reduces the amount of heat for calcium looping calciner and clinker production kiln. The cost of clinker production, after applying the carbon tax, for coal-fired and hydrogen-fueled ones is obtained respectively at 131.21 USD and 249.18 USD. text
institution Institut Teknologi Bandung
building Institut Teknologi Bandung Library
continent Asia
country Indonesia
Indonesia
content_provider Institut Teknologi Bandung
collection Digital ITB
language Indonesia
topic Teknik (Rekayasa, enjinering dan kegiatan berkaitan)
spellingShingle Teknik (Rekayasa, enjinering dan kegiatan berkaitan)
Izzatur Rahman, Labib
DOMAIN-SPECIFIC LANGUAGE DEVELOPMENT FOR SMART CONTRACT SPECIFICATIONS
description CO2 emissions have negative impacts on the environment, one of which is global warming. The cement production process accounts for 5% of global CO2 emissions. The increase in CO2 emissions from the cement production process continues. Carbon capture has potential to be the solution to reduce CO2 emissions from cement factories. The carbon capture method that will be discussed in this final project is calcium looping. Calcium looping consists of two simple reactors consisting of a carbonator and calciner. Calcium looping material can be used as raw material for cement. The analysis was carried out by modeling and simulating the cement production process at Factory Pabrik V Indarung PT. Semen Indonesia. Simulations were carried out with Aspen Plus Ver. 11 software. The simulation of the application of calcium looping is carried out by adding carbonator and calciner components and making changes to the system as needed. The reduction in CO2 emissions after the calcium looping was applied is 37% for the coal fired system and 99% for the hydrogen fueled system. Fuel requirements increased by 94 kg/kg clinker for coal fired systems and 154 kg/kg clinker for hydrogen fueled systems. In addition, the increase in the ratio of the mole flow rate of CaCO3 added to the calcium looping to the mole flow rate of CO2 emissions (Fo/FCO2) reduces the amount of heat for calcium looping calciner and clinker production kiln. The cost of clinker production, after applying the carbon tax, for coal-fired and hydrogen-fueled ones is obtained respectively at 131.21 USD and 249.18 USD.
format Theses
author Izzatur Rahman, Labib
author_facet Izzatur Rahman, Labib
author_sort Izzatur Rahman, Labib
title DOMAIN-SPECIFIC LANGUAGE DEVELOPMENT FOR SMART CONTRACT SPECIFICATIONS
title_short DOMAIN-SPECIFIC LANGUAGE DEVELOPMENT FOR SMART CONTRACT SPECIFICATIONS
title_full DOMAIN-SPECIFIC LANGUAGE DEVELOPMENT FOR SMART CONTRACT SPECIFICATIONS
title_fullStr DOMAIN-SPECIFIC LANGUAGE DEVELOPMENT FOR SMART CONTRACT SPECIFICATIONS
title_full_unstemmed DOMAIN-SPECIFIC LANGUAGE DEVELOPMENT FOR SMART CONTRACT SPECIFICATIONS
title_sort domain-specific language development for smart contract specifications
url https://digilib.itb.ac.id/gdl/view/71717
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