MY176872A - Gasification apparatus with supercritical fluid - Google Patents

Gasification apparatus with supercritical fluid

Info

Publication number
MY176872A
MY176872A MYPI2016703206A MYPI2016703206A MY176872A MY 176872 A MY176872 A MY 176872A MY PI2016703206 A MYPI2016703206 A MY PI2016703206A MY PI2016703206 A MYPI2016703206 A MY PI2016703206A MY 176872 A MY176872 A MY 176872A
Authority
MY
Malaysia
Prior art keywords
gasification
feedstock
treated fluid
gasification feedstock
flow channel
Prior art date
Application number
MYPI2016703206A
Inventor
Yasutaka Wada
Haruhito Kubota
Yukimasa Yamamura
Ichiro Uchiyama
Keiji Oyama
Toshiki Yamasaki
Yukihiko Matsumura
Yoshifumi Kawai
Takashi Noguchi
Original Assignee
Chugoku Electric Power
Univ Hiroshima
Toyo Koatsu Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Chugoku Electric Power, Univ Hiroshima, Toyo Koatsu Co Ltd filed Critical Chugoku Electric Power
Priority to MYPI2016703206A priority Critical patent/MY176872A/en
Priority claimed from PCT/JP2014/055695 external-priority patent/WO2015132922A1/en
Publication of MY176872A publication Critical patent/MY176872A/en

Links

Abstract

[PROBLEM] In a gasification apparatus that heats and pressurizes a gasification feedstock to bring the gasification feedstock into a fluid in a supercritical state and performs decomposition-treatment on the gasification feedstock to obtain fuel gas, energy possessed by the treated fluid can be effectively utilized. [SOLUTION] A gasification apparatus configured to heat and pressurize a gasification feedstock to bring the gasification feedstock into a supercritical state, and perform decomposition-treatment on the gasification feedstock to obtain fuel gas. the gasification apparatus including: a heat exchanger (31) configured to introduce the gasification feedstock into a low-temperature-side flow channel (31a) and introduce treated fluid in a supercritical state into a high-temperature-side flow channel (31 b), so that heat exchange is performed between the gasification feedstock and the treated fluid; a gas-liquid separator (51) configured to extract from the high-temperature-side flow channel (31 b). the treated fluid that has been in a subcritical state due to heat exchange. perform gas-liquid separation on the treated fluid, and return a separated liquid to the high-temperature-side flow channel (31 b); and a synthesis device (52) configured to synthesize a liquid fuel from fuel gas separated by the gas-liquid separator (51).
MYPI2016703206A 2014-03-05 2014-03-05 Gasification apparatus with supercritical fluid MY176872A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
MYPI2016703206A MY176872A (en) 2014-03-05 2014-03-05 Gasification apparatus with supercritical fluid

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
MYPI2016703206A MY176872A (en) 2014-03-05 2014-03-05 Gasification apparatus with supercritical fluid
PCT/JP2014/055695 WO2015132922A1 (en) 2014-03-05 2014-03-05 Apparatus for gasification with supercritical fluid

Publications (1)

Publication Number Publication Date
MY176872A true MY176872A (en) 2020-08-25

Family

ID=79730755

Family Applications (1)

Application Number Title Priority Date Filing Date
MYPI2016703206A MY176872A (en) 2014-03-05 2014-03-05 Gasification apparatus with supercritical fluid

Country Status (1)

Country Link
MY (1) MY176872A (en)

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