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1. 发明专利

AU2002300204B2 Method of manufacturing methanol 未知
公开(公告)号：AU2002300204B2
公开(公告)日：2004-11-18
申请号：AU2002300204
申请日：2002-07-19
申请人： MITSUBISHI GAS CHEMICAL CO , MITSUBISHI HEAVY IND ENG LTD
发明人： SEIKI YOSHIO , MIYAMOTO SHUICHI , MORITA KAZUHIRO , KUWADA CHIE , OSORA HIROYUKI , KOBAYASHI KAZUTO , IMAI TETSUYA
IPC分类号： C07C29/152 , C07B61/00 , C07C29/151 , C07C31/04 , C07C029/151
摘要： A method of manufacturing methanol comprising reacting hydrocarbons with water vapor in a reformer (10) to produce a synthesis gas containing hydrogen, carbon monoxide and carbon dioxide, allowing reaction of the synthesis gas to take place over a methanol-synthesizing catalyst to produce a crude methanol, cooling the crude methanol, separating the cooled crude methanol into unreacted gas and liquid crude methanol, and distilling the liquid crude methanol to separate it into refined methanol and waste water containing low boiling point organic compounds and high boiling point organic compounds. Carbon dioxide in combustion exhaust gas to be discharged from the reformer (10) is recovered in a carbon dioxide-recovering device, and that in feeding the carbon dioxide thus recovered to the upstream side and/or the downstream side of the reformer (10), part of the unreacted gas is utilized as a purge gas, a portion of which being utilized as a fuel for a combustion device (12) of the reformer (10), while the balance of the purge gas being utilized as a fuel for other heating sources and/or as an agent for desulfurizating raw gas. Producing a synthesis gas containing hydrogen, carbon monoxide and carbon dioxide, allowing reaction of the synthesis gas to take place over a catalyst to produce a crude methanol, separating the crude methanol into unreacted gas and liquid crude methanol, and distilling the liquid crude methanol to separate it into refined methanol and waste water. Carbon dioxide in combustion exhaust gas to be discharged from a reformer (10) is recovered, and that in feeding the carbon dioxide to the upstream side and/or the downstream side of the reformer (10), part of the unreacted gas is utilized as a purge gas, a portion of which being utilized as a fuel for a combustion device (12) of the reformer (10), while the balance of the purge gas being utilized as a fuel for other heating sources and/or as an agent for desulfurizating raw gas.

2. 发明专利

AU2002300205B2 Method of manufacturing methanol 未知
公开(公告)号：AU2002300205B2
公开(公告)日：2004-06-03
申请号：AU2002300205
申请日：2002-07-19
申请人： MITSUBISHI GAS CHEMICAL CO , MITSUBISHI HEAVY IND ENG LTD
发明人： KUWADA CHIE , OSORA HIROYUKI , KOBAYSHI KAZUTO , IMAI TETSUYA , SEIKI YOSHIO , MIYAMOTO SHUICHI , MORITA KAZUHIRO
IPC分类号： B01D53/14 , C01B3/38 , C01B32/40 , C01B32/50 , C07B61/00 , C07C29/151 , C07C29/152 , C07C29/80 , C07C31/04 , C07C029/151
摘要： A method of manufacturing methanol comprising reacting hydrocarbons with water vapor in a reformer (30) to produce a synthesis gas containing hydrogen, carbon monoxide and carbon dioxide, recovering carbon dioxide from combustion exhaust gas which has been discharged from the reformer (30) by a carbon dioxide recovery apparatus (90) provided with a carbon dioxide absorption tower and with a carbon dioxide-absorbing solution regenerating tower, feeding the carbon dioxide thus recovered to the upstream side and/or the downstream side of the reformer (30), allowing reaction of the synthesis gas to take place over a catalyst to produce a reaction product, recovering liquid crude methanol from the reaction product, distilling the liquid crude methanol in a distillation apparatus (80) provided with a pressure distillation tower and with an atmospheric distillation tower to separate it into refined methanol and waste water containing low boiling point organic compounds and high boiling point organic compounds. Bottom liquid in a topping tower of the distillation apparatus (80) is heated and introduced into the pressure distillation tower in the distillation step, and the heat of distilled liquid discharged from the top of the pressure distillation tower is utilized as a heat source for the carbon dioxide-absorbing solution regenerating tower (93) and as a heat source for the atmospheric distillation tower.

3. 发明专利

DK3190088T3 FREMGANGSMÅDE TIL SYNTESE AF AMMONIAK 未知
公开(公告)号：DK3190088T3
公开(公告)日：2019-09-02
申请号：DK15837863
申请日：2015-04-21
申请人： MITSUBISHI HEAVY IND ENG LTD
发明人： SAKURAI MIKIYA , TANAKA YUKIO , OKUZUMI NAOYA , OSORA HIROYUKI , HIRAYAMA HARUAKI
IPC分类号： C01C1/02 , B01J23/46 , C01C1/04

4. 发明专利

AU6437099A Method of manufacturing methanol 未知
公开(公告)号：AU6437099A
公开(公告)日：2000-06-22
申请号：AU6437099
申请日：1999-12-07
申请人： MITSUBISHI HEAVY IND ENG LTD
发明人： KOBAYASHI KAZUTO , IMAI TETSUYA , SEIKI YOSHIO , OSORA HIROYUKI , NAGAI HIDEAKI
IPC分类号： C07C29/151 , C07C29/154 , C07C31/04
摘要： A raw material gas containing hydrocarbon as a main component is supplied together with steam to a reformer (20) through a moistening device (10) to form a synthetic gas containing hydrogen, carbon monoxide and carbon dioxide as main components by the reaction between the hydrocarbon contained in the raw material gas and the steam. In forming the synthetic gas, carbon dioxide is supplied to at least one fluid passageway selected from the group consisting of the fluid passageway (306) positioned upstream of the moistening device (10) and the fluid passageway (301) interposed between the moistening device (10) and the reformer (20). As a result, the excess hydrogen contained in the gas formed in the reformer (20) is effectively utilized without bringing about deactivation of the methanol synthesizing catalyst in the methanol synthesizing step. Also, carbon dioxide is effectively utilized to decrease the amount of carbon dioxide discharged to the outside of the system. Further, it is possible to decrease the amount of steam supplied to the reformer (20).

5. 发明专利

DK1277722T3 未知
公开(公告)号：DK1277722T3
公开(公告)日：2005-04-25
申请号：DK02016115
申请日：2002-07-19
申请人： MITSUBISHI HEAVY IND LTD , MITSUBISHI GAS CHEMICAL CO
发明人： SEIKI YOSHIO , IMAI TETSUYA , KOBAYASHI KAZUTO , OSORA HIROYUKI , KUWADA CHIE , MORITA KAZUHIRO , MIYAMOTO SHUICHI
IPC分类号： B01D53/14 , C01B3/38 , C01B32/40 , C01B32/50 , C07B61/00 , C07C29/151 , C07C29/152 , C07C29/80 , C07C31/04 , C01B31/20
摘要： A method of manufacturing methanol comprising reacting hydrocarbons with water vapor in a reformer (30) to produce a synthesis gas containing hydrogen, carbon monoxide and carbon dioxide, recovering carbon dioxide from combustion exhaust gas which has been discharged from the reformer (30) by a carbon dioxide recovery apparatus (90) provided with a carbon dioxide absorption tower and with a carbon dioxide-absorbing solution regenerating tower, feeding the carbon dioxide thus recovered to the upstream side and/or the downstream side of the reformer (30), allowing reaction of the synthesis gas to take place over a catalyst to produce a reaction product, recovering liquid crude methanol from the reaction product, distilling the liquid crude methanol in a distillation apparatus (80) provided with a pressure distillation tower and with an atmospheric distillation tower to separate it into refined methanol and waste water containing low boiling point organic compounds and high boiling point organic compounds. Bottom liquid in a topping tower of the distillation apparatus (80) is heated and introduced into the pressure distillation tower in the distillation step, and the heat of distilled liquid discharged from the top of the pressure distillation tower is utilized as a heat source for the carbon dioxide-absorbing solution regenerating tower (93) and as a heat source for the atmospheric distillation tower.

6. 发明专利

AU2002300206B2 Method for manufacturing synthesis gas and method for manufacturing methanol 未知
公开(公告)号：AU2002300206B2
公开(公告)日：2004-05-27
申请号：AU2002300206
申请日：2002-07-19
申请人： MITSUBISHI GAS CHEMICAL CO , MITSUBISHI HEAVY IND LTD
发明人： MIYAMOTO SHUICHI , MORITA KAZUHIRO , KUWADA CHIE , OSORA HIROYUKI , KOBAYASHI KAZUTO , IMAI TETSUYA , SEIKI YOSHIO
IPC分类号： B01D53/14 , C01B3/38 , C01B3/52 , C01B32/50 , C07C29/151 , C07C29/152 , C07C31/04 , C01B003/34

7. 发明专利

DE60203761T2 未知
公开(公告)号：DE60203761T2
公开(公告)日：2006-03-02
申请号：DE60203761
申请日：2002-07-19
申请人： MITSUBISHI GAS CHEMICAL CO , MITSUBISHI HEAVY IND LTD
发明人： SEIKI YOSHIO , IMAI TETSUYA , KOBAYASHI KAZUTO , OSORA HIROYUKI , KUWADA CHIE , MORITA KAZUHIRO , MIYAMOTO SHUICHI
IPC分类号： B01D53/14 , C01B3/38 , C01B3/52 , C01B32/50 , C07C29/151 , C07C29/152 , C07C31/04

8. 发明专利

DE60203569D1 未知
公开(公告)号：DE60203569D1
公开(公告)日：2005-05-12
申请号：DE60203569
申请日：2002-07-19
申请人： MITSUBISHI GAS CHEMICAL CO , MITSUBISHI HEAVY IND LTD
发明人： SEIKI YOSHIO , IMAI TETSUYA , KOBAYASHI KAZUTO , OSORA HIROYUKI , KUWADA CHIE , MORITA KAZUHIRO , MIYAMOTO SHUICHI
IPC分类号： B01D53/14 , C01B3/38 , C01B32/40 , C01B32/50 , C07B61/00 , C07C29/151 , C07C29/152 , C07C29/80 , C07C31/04 , C01B31/20
摘要： A method of manufacturing methanol comprising reacting hydrocarbons with water vapor in a reformer (30) to produce a synthesis gas containing hydrogen, carbon monoxide and carbon dioxide, recovering carbon dioxide from combustion exhaust gas which has been discharged from the reformer (30) by a carbon dioxide recovery apparatus (90) provided with a carbon dioxide absorption tower and with a carbon dioxide-absorbing solution regenerating tower, feeding the carbon dioxide thus recovered to the upstream side and/or the downstream side of the reformer (30), allowing reaction of the synthesis gas to take place over a catalyst to produce a reaction product, recovering liquid crude methanol from the reaction product, distilling the liquid crude methanol in a distillation apparatus (80) provided with a pressure distillation tower and with an atmospheric distillation tower to separate it into refined methanol and waste water containing low boiling point organic compounds and high boiling point organic compounds. Bottom liquid in a topping tower of the distillation apparatus (80) is heated and introduced into the pressure distillation tower in the distillation step, and the heat of distilled liquid discharged from the top of the pressure distillation tower is utilized as a heat source for the carbon dioxide-absorbing solution regenerating tower (93) and as a heat source for the atmospheric distillation tower.

9. 发明专利

AU2002301014B2 Reacting method 未知
公开(公告)号：AU2002301014B2
公开(公告)日：2004-03-11
申请号：AU2002301014
申请日：2002-09-13
申请人： MITSUBISHI GAS CHEMICAL CO , MITSUBISHI HEAVY IND LTD
发明人： IMAI TETSUYA , SEIKI YOSHIO , OSORA HIROYUKI , MIYAMOTO SHUICHI , MORITA KAZUHIRO , KUWADA CHIE , KOBAYASHI KAZUTO
IPC分类号： B01J23/835 , B01J8/00 , B01J8/04 , B01J8/06 , B01J23/80 , C07B61/00 , C07C29/151 , C07C29/152 , C07C29/154 , C07C31/04 , C21B13/00 , B01J008/06 , B01J008/02

10. 发明专利

DE60203569T2 未知
公开(公告)号：DE60203569T2
公开(公告)日：2006-02-09
申请号：DE60203569
申请日：2002-07-19
申请人： MITSUBISHI GAS CHEMICAL CO , MITSUBISHI HEAVY IND LTD
发明人： SEIKI YOSHIO , IMAI TETSUYA , KOBAYASHI KAZUTO , OSORA HIROYUKI , KUWADA CHIE , MORITA KAZUHIRO , MIYAMOTO SHUICHI
IPC分类号： B01D53/14 , C01B3/38 , C01B32/40 , C01B32/50 , C07B61/00 , C07C29/151 , C07C29/152 , C07C29/80 , C07C31/04
摘要： A method of manufacturing methanol comprising reacting hydrocarbons with water vapor in a reformer (30) to produce a synthesis gas containing hydrogen, carbon monoxide and carbon dioxide, recovering carbon dioxide from combustion exhaust gas which has been discharged from the reformer (30) by a carbon dioxide recovery apparatus (90) provided with a carbon dioxide absorption tower and with a carbon dioxide-absorbing solution regenerating tower, feeding the carbon dioxide thus recovered to the upstream side and/or the downstream side of the reformer (30), allowing reaction of the synthesis gas to take place over a catalyst to produce a reaction product, recovering liquid crude methanol from the reaction product, distilling the liquid crude methanol in a distillation apparatus (80) provided with a pressure distillation tower and with an atmospheric distillation tower to separate it into refined methanol and waste water containing low boiling point organic compounds and high boiling point organic compounds. Bottom liquid in a topping tower of the distillation apparatus (80) is heated and introduced into the pressure distillation tower in the distillation step, and the heat of distilled liquid discharged from the top of the pressure distillation tower is utilized as a heat source for the carbon dioxide-absorbing solution regenerating tower (93) and as a heat source for the atmospheric distillation tower.

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