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公开(公告)号:DE69711575D1
公开(公告)日:2002-05-08
申请号:DE69711575
申请日:1997-12-15
Applicant: AGENCY IND SCIENCE TECHN
Inventor: SAKO TAKESHI , SATO MASAHITO , SUGETA TSUTOMU , OTAKE KATSUTO , OKANO MAKOTO
IPC: A62D3/20 , A62D101/22 , A62D3/00
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公开(公告)号:DE10006903A1
公开(公告)日:2000-11-23
申请号:DE10006903
申请日:2000-02-16
Applicant: AGENCY IND SCIENCE TECHN , SHIN NIPPON AIR TECH CO LTD
Inventor: SAKO TAKESHI , GODO MASAZUMI , ISHIDA SEIJI , MIURA KUNIO , TSUGUMI MASAYUKI
IPC: C07C27/02 , C07C29/128 , C07C67/03 , C07C69/773 , C07C67/00 , C07C67/48 , C07C69/82 , C07C29/74 , C07C31/20 , C07B37/06 , B09B3/00
Abstract: A process for the continuous production of monomer components of an aromatic polyester, by reaction of the aromatic polyester (A) with a super critical alcohol (B) to form an aromatic divalent carboxylic acid ester (C) and a divalent alcohol (D) is carried out in a reactor which is maintained under supercritical conditions for (B). A process for the continuous production of monomer components of an aromatic polyester, by reaction of the aromatic polyester (A) with a super critical alcohol (B) to form an aromatic divalent carboxylic acid ester (C) and a divalent alcohol (D) comprises continuous addition of the aromatic polyester (A) and the monovalent alcohol (B) into a reactor which is maintained under supercritical conditions for (B); reaction of (A) and (B) with continuous removal of (C), (D) and (B) from the reactor and separation and recovery of (C) and (D).
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公开(公告)号:DE19712045A1
公开(公告)日:1997-12-11
申请号:DE19712045
申请日:1997-03-21
Applicant: AGENCY IND SCIENCE TECHN
Inventor: SAKO TAKESHI , SATO MASAHITO , SUGETA TSUTOMU , OTAKE KATSUTO , TSUGUMI MASAYUKI
IPC: A62D3/20 , A62D3/38 , A62D101/08 , A62D101/22 , A62D101/26 , A62D101/28 , B09B3/00 , A62D3/00
Abstract: A method of decomposing dioxin compounds, such as polychlorodibenzo-p-dioxins and polychlorodibenzofurans, contained in a waste material into unharmful substances, wherein the waste material is treated with a supercritical water at a temperature higher than the critical temperature of water and a pressure higher than the critical pressure of water.
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公开(公告)号:DE69711575T2
公开(公告)日:2002-11-28
申请号:DE69711575
申请日:1997-12-15
Applicant: AGENCY IND SCIENCE TECHN
Inventor: SAKO TAKESHI , SATO MASAHITO , SUGETA TSUTOMU , OTAKE KATSUTO , OKANO MAKOTO
IPC: A62D3/20 , A62D101/22 , A62D3/00
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公开(公告)号:GB2314079B
公开(公告)日:2000-06-28
申请号:GB9706070
申请日:1997-03-24
Applicant: AGENCY IND SCIENCE TECHN
Inventor: SAKO TAKESHI , SATO MASAHITO , SUGETA TSUTOMU , OTAKE KATSUTO , TSUGUMI MASAYUKI
IPC: A62D3/20 , A62D3/38 , A62D101/08 , A62D101/22 , A62D101/26 , A62D101/28 , B09B3/00 , A62D3/00
Abstract: A method of decomposing dioxin compounds, such as polychlorodibenzo-p-dioxins and polychlorodibenzofurans, contained in a waste material into unharmful substances, wherein the waste material is treated with a supercritical water at a temperature higher than the critical temperature of water and a pressure higher than the critical pressure of water.
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公开(公告)号:GB2314079A
公开(公告)日:1997-12-17
申请号:GB9706070
申请日:1997-03-24
Applicant: AGENCY IND SCIENCE TECHN
Inventor: SAKO TAKESHI , SATO MASAHITO , SUGETA TSUTOMU , OTAKE KATSUTO , TSUGUMI MASAYUKI
IPC: A62D3/20 , A62D3/38 , A62D101/08 , A62D101/22 , A62D101/26 , A62D101/28 , B09B3/00 , A62D3/00
Abstract: A method of decomposing dioxin compounds, such as polychlorodibenzo-p-dioxins and polychlorodibenzofurans, contained in a waste material into unharmful substances, wherein the waste material is treated with a supercritical water at a temperature higher than the critical temperature of water and a pressure higher than the critical pressure of water.
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公开(公告)号:JPH11217346A
公开(公告)日:1999-08-10
申请号:JP1894998
申请日:1998-01-30
Applicant: AGENCY IND SCIENCE TECHN , SUMITOMO CHEMICAL CO
Inventor: SUZUKI TOMOYUKI , OKADA AKIHIKO , SAKO TAKESHI
IPC: C07C41/50 , C07C43/303
Abstract: PROBLEM TO BE SOLVED: To obtain an acetal by a simple and inexpensive method without requiring a catalyst, by reacting a carbonyl group-containing organic compound with a lower alcohol under conditions to make the carbonyl group-containing organic compound and the lower alcohol in a supercritical state. SOLUTION: (A) A carbonyl group-containing organic compound a compound of the formula [R1 and R2 are each H or a (substituted) hydrocarbyl or R1 and R2 are mutually bonded partially to form a cyclic structure] such as a ketone, e.g. acetone or the like or an aldehyde, e.g. acetaldehyde or the like} is reacted with (B) a lower alcohol [a monohydric lower alcohol of the formula R3 -OH (R3 is a 1-10C hydrocarbyl) or a dihydric lower alcohol such as ethylene glycol or the like] preferably in the presence of (C) an inert medium such as carbon dioxide or the like under conditions to make the carbonyl group- containing organic compound and/or the lower alcohol (and/or the inert medium) in a supercritical state.
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公开(公告)号:JPH10225632A
公开(公告)日:1998-08-25
申请号:JP11596697
申请日:1997-05-07
Applicant: AGENCY IND SCIENCE TECHN
Inventor: SAKO TAKESHI , SATO SHINJI , SUGATA TAKESHI , OTAKE KATSUTO , OKANO MAKOTO
Abstract: PROBLEM TO BE SOLVED: To detoxicate polychlorinated biphenyl by decomposing it with supercritical water alone, supercritical water admixed with alkali or supercritical water admixed with alkali and an oxidizing agent. SOLUTION: About 50-150 weight units of water, based on one weight unit of PCB, 50-150 weight units of water and 1-5 weight units of such an alkali as sodium hydroxide or 50-150 weight units of water, 2-20 weight units of an oxidizing agent such as hydrogen peroxide and 1-5 weight units of an alkali such as sodium hydroxide are filled in a reactor and heated above the critical temp. of water in a heating furnace. The reaction pressure is adjusted in accordance with the weight of water filled in the reactor, and the reaction time is controlled to 5-60min. Oxygen, air, etc., are used as the oxidizing agent as well as hydrogen peroxide. Sodium carbonate is used as the alkali besides sodium hydroxide. Consequently, the high reaction temp. and long reaction time are not needed to make polychlorinated biphenyl harmless without causing the resynthesis of PCB.
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公开(公告)号:JPH09249597A
公开(公告)日:1997-09-22
申请号:JP5562596
申请日:1996-03-13
Applicant: AGENCY IND SCIENCE TECHN
Inventor: SAKO TAKESHI , SATO SHINJI , SUGATA TAKESHI , OTAKE KATSUTO
Abstract: PROBLEM TO BE SOLVED: To decompose an aromatic polyester into an aromatic dihydric carboxylic acid in a form of methyl ester and a dihydric alcohol in a short time and recover these monomers in a high yield by reacting the aromatic polyester with a supercritical methanol. SOLUTION: An aromatic polyester (e.g. polyethylene terephthalate) is reacted with a supercritical methanol to provide dimethyl aromatic dihydric carboxylic acid and a dihydric alcohol. The reaction is preferably carried out by packing the aromatic polyester and methanol into a reactor and heating the reactor under supercritical conditions of methanol. The supercritical conditions are preferably 523-653K deg. temperature and 5 to 25MP pressure. Methanol is preferably used in a ratio of 20-70mol based on 1mol aromatic dihydric carboxylic aid contained in the aromatic polyester. The aromatic dihydric carboxylic acid dimethyl ester and the dihydric alcohol can be recovered from the reaction product in high purity from a method such as distillation or crystallization.
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公开(公告)号:JPH03287550A
公开(公告)日:1991-12-18
申请号:JP8873890
申请日:1990-04-03
Applicant: AGENCY IND SCIENCE TECHN
Inventor: SAKO TAKESHI , SATO SHINJI , SUGATA TAKESHI , NAKAZAWA NOBUAKI , YAMANE SUMIYO
Abstract: PURPOSE:To safely, inexpensively and simply separate a polycyclic aromatic compound in a energy-saving state from a mixture such as petroleum refined oil or coal tar with supercritical carbon dioxide as a extraction and crystallization solvent. CONSTITUTION:A raw material mixture is charged into an extraction tank 7 and super critical carbon dioxide is fed into the extraction tank 7 through a high pressure pump 2 and a pre-heating coil 5 to extract the mixture with the super critical carbon dioxide. The temperature and pressure of the extraction tank 7 are controlled with an air constant temperature bath and a back pressure valve 3. After the extraction the super critical fluid containing the mixture is fed from the constant temperature tank 10 into a crystallization tank 12 maintained at a prescribed temperature and only the objective component in the mixture is deposited. The super critical fluid containing the solutes in the crystallization tank is substituted with the pure super critical fluid and subsequently the pressure in the tank is reduced to the atmospheric pressure to recover the component. Since the process can be operated at a relatively low temperature, the pyrolysis and polymerization of the target substance can be prevented.
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