• Title/Summary/Keyword: tri-reformer

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The Study of KOGAS DME Process in Small and Medium Sized Gas Field Containing $CO_2$ ($CO_2$가 함유된 중소규모 가스전을 위한 KOGAS DME Process 연구)

  • Mo, Yong-Gi;Cho, Won-Jun;Song, Taek-Yong;Baek, Young-Soon
    • Journal of the Korean Institute of Gas
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    • v.14 no.4
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    • pp.51-55
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    • 2010
  • The global activities to reduce the $CO_2$ emission as a greenhouse gas have been various efforts. Under this circumstance, small and medium sized gas field containing $CO_2$ to develop as LNG is not economic feasibility. Particularly, for the separation of $CO_2$ in gas field, separation facilities should be installed to add. This is and increase in plant construction cost and separated $CO_2$ emission into the atmosphere is not the result of greenhouse gas reduction. When the uneconomic gas field apply the KOGAS DME process, the gas field containing $CO_2$ can be increase economic feasibility because of natural gas and $CO_2$ can be use to resource gas. The Tri-reformer produced syngas as H2 and CO in KOGAS DME process and the resource gases are natural gas, steam, oxygen and $CO_2$. The $CO_2$ is used as raw material gases from recover $CO_2$ in DME process. In this study, we investigated range of application of $CO_2$ in gas field.

Production of DME from CBM by KOGAS DME Process (KOGAS DME 공정을 이용한 CBM으로부터 DME 생산)

  • Cho, Won-Jun;Mo, Yong-Gi;Song, Taek-Yong;Lee, Hyen-Chan;Baek, Young-Soon;Denholm, Douglas;Ko, Glen;Choi, Chang-Woo
    • Journal of Hydrogen and New Energy
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    • v.22 no.6
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    • pp.925-933
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    • 2011
  • The traditional feedstock for dimethyl ether (DME) has been natural gas obtained by pipeline from a nearby natural gas or oil field. This report focuses on other feedstock: Coal bed methane (CBM). The resource availability and suitability of CBM for DME manufacturing have been investigated. CBM in a short time has become an important industry, providing an abundant clean-burning fuel and also suggesting as a feedstock for gas industry. The use of CBM will have very little impact on the KOGAS' DME process design and economics up to 50 vol% of $CO_2$ in the CBM source. Many of the CBM sources in Asia are high in $CO_2$, but pose no difficulties for the KOGAS' DME plant. Since tri-reformer requires substantial $CO_2$ in its feed, no $CO_2$ removal from the CBM feed is needed. The $CO_2$ in the CBM means that less $CO_2$ needs to be recycled from the downstream in the process.

Optimization of KOGAS DME Process From Demonstration Long-Term Test (KOGAS DME 공정의 실증 시험을 통한 최적화 기술개발)

  • Chung, Jongtae;Cho, Wonjun;Baek, Youngsoon;Lee, Changha
    • Journal of Hydrogen and New Energy
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    • v.23 no.5
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    • pp.559-571
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    • 2012
  • Dimethyl ether (DME) is a new clean fuel as an environmentally-benign energy resource. DME can be manufactured from various energy sources including natural gas, coal, and biomass. In addition to its environmentally friendly properties, DME has similar characteristics to those of LPG. The aim of this article is to represent the development of new DME process with KOGAS's own technologies. KOGAS has investigated and developed new innovative DME synthesis process from synthesis gas in gaseous phase fixed bed reactor. DME has been traditionally produced by the dehydration of methanol which is produced from syngas, a product of natural gas reforming. This traditional process is thus called the two-step method of preparing DME. However, DME can also be manufactured directly from syngas (single-step). The single-step method needs only one reactor for the synthesis of DME, instead of two for the two-step process. It can also alleviate the thermodynamic limitations associated with the synthesis of methanol, by converting the produced methanol into DME, thereby potentially enhancing the overall conversion of syngas into DME. KOGAS had launched the 10 ton/day DME demonstration plant project in 2004 at Incheon KOGAS LNG terminal. In the mid of 2008, KOGAS had finished the construction of this plant and has successively finished the demonstration plant operation. And since 2008, we have established the basic design of commercial plant which can produce 3,000 ton/day DME.