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公开(公告)号:CA2452846A1
公开(公告)日:2003-03-20
申请号:CA2452846
申请日:2002-06-26
Applicant: TEXACO DEVELOPMENT CORP
Inventor: VUONG DINH-CUONG
Abstract: An integrated reactor and solids settler system for solids removal from a water stream. An overflow line (123) from the rapid mix reactor (114) is use d to eliminate both the rapid mix reactor level indicator and controller, and the flow controller in the solids settler (130) clarified water outlet (136) .
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公开(公告)号:CA2260205C
公开(公告)日:2002-06-04
申请号:CA2260205
申请日:1997-07-14
Applicant: TEXACO DEVELOPMENT CORP
Inventor: WEBSTER GEORGE HENRY JR , VUONG DINH-CUONG , JOHNSON STEVEN ROBERT , STEVENSON JOHN SAUNDERS , VON KLOCK BYRON
Abstract: The invention relates to a process for minimizing evaporator scaling during the recovery of liquids and solids from the aqueous effluent discharged duri ng a partial oxidation gasification from a gasifier (16), wherein the aqueous effluent contains ammonium chloride. The aqueous effluent is evaporated in a n evaporator (106) to produce a distillate water line (110) and a line containing brine (112) with a brine concentration of about 10 to 60 weight percent. The brine can be further concentrated and ammonium chloride crystal s are recovered. The distillate is recycled to the gasification reaction. No effluent discharges to the environment.
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公开(公告)号:DE69521528D1
公开(公告)日:2001-08-02
申请号:DE69521528
申请日:1995-12-27
Applicant: TEXACO DEVELOPMENT CORP
Inventor: BROOKER DONALD , FALSETTI SAMUEL , WOLFENBARGER KENNETH , VUONG DINH-CUONG
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公开(公告)号:ES2146738T3
公开(公告)日:2000-08-16
申请号:ES95902624
申请日:1994-11-18
Applicant: TEXACO DEVELOPMENT CORP
Inventor: BROOKER DUANE DONALD , FALSETTI JAMES SAMUEL , WOLFENBARGER JAMES KENNETH , VUONG DINH-CUONG
IPC: F23J1/02 , B01J7/00 , C10J3/00 , C10J3/20 , C10J3/48 , C10J3/72 , C10J3/76 , C10K1/00 , F23G5/12 , F23J1/08 , B01J8/04 , C10J3/68 , F22B37/00
Abstract: A gasifier for partially combusting a carbonaceous fuel mixture in the combustion chamber of the gasifier. The latter includes a water bath into which the hot effluent or products of combustion are immersed, including a synthetic gas. The products of combustion are directed into the bath by way of a constricted throat section. To avoid excessive erosion action and/or thermal shock to the throat section as a result of exposure to the effluent's high temperatures, the throat section is structured with an internal framework of pipes. The framework is communicated with a pressurized source of a cooling fluid, preferably water, whereby to cool the throat section sufficiently to counteract the ill effects of exposure to contact with the high temperature effluent.
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公开(公告)号:DE69424878D1
公开(公告)日:2000-07-13
申请号:DE69424878
申请日:1994-11-18
Applicant: TEXACO DEVELOPMENT CORP
Inventor: BROOKER DONALD , FALSETTI SAMUEL , WOLFENBARGER KENNETH , VUONG DINH-CUONG
IPC: F23J1/02 , B01J7/00 , C10J3/00 , C10J3/20 , C10J3/48 , C10J3/72 , C10J3/76 , C10K1/00 , F23G5/12 , F23J1/08 , B01J8/04 , C10J3/68 , F22B37/00
Abstract: A gasifier for partially combusting a carbonaceous fuel mixture in the combustion chamber of the gasifier. The latter includes a water bath into which the hot effluent or products of combustion are immersed, including a synthetic gas. The products of combustion are directed into the bath by way of a constricted throat section. To avoid excessive erosion action and/or thermal shock to the throat section as a result of exposure to the effluent's high temperatures, the throat section is structured with an internal framework of pipes. The framework is communicated with a pressurized source of a cooling fluid, preferably water, whereby to cool the throat section sufficiently to counteract the ill effects of exposure to contact with the high temperature effluent.
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公开(公告)号:CZ9900147A3
公开(公告)日:1999-06-16
申请号:CZ14799
申请日:1997-07-14
Applicant: TEXACO DEVELOPMENT CORP
Inventor: WEBSTER GEORGE HENRY JR , VON KLOCK BYRON , VUONG DINH-CUONG , STEVENSON JOHN SAUNDERS , JOHNSON STEVEN ROBERT
CPC classification number: C01C1/164 , C01B3/52 , C01B2203/0415 , C01B2203/0465 , C01B2203/0485 , C01B2203/0495 , C02F1/042 , C10J3/466 , C10J3/84 , C10J2300/0926 , C10J2300/093 , C10J2300/169 , C10J2300/1807 , C10J2300/1846 , C10K1/00 , C10K1/002 , C10K1/10 , C10K1/101 , Y10S159/13
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公开(公告)号:CA2260205A1
公开(公告)日:1998-01-22
申请号:CA2260205
申请日:1997-07-14
Applicant: TEXACO DEVELOPMENT CORP
Inventor: JOHNSON STEVEN ROBERT , STEVENSON JOHN SAUNDERS , VUONG DINH-CUONG , VON KLOCK BYRON , WEBSTER GEORGE HENRY JR
Abstract: The invention relates to a process for minimizing evaporator scaling during the recovery of liquids and solids from the aqueous effluent discharged during a partial oxidation gasification from a gasifier (16), wherein the aqueous effluent contains ammonium chloride. The aqueous effluent is evaporated in an evaporator (106) to produce a distillate water line (110) and a line containing brine (112) with a brine concentration of about 10 to 60 weight percent. The brine can be further concentrated and ammonium chloride crystals are recovered. The distillate is recycled to the gasification reaction. No effluent discharges to the environment.
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公开(公告)号:SK66596A3
公开(公告)日:1997-08-06
申请号:SK66596
申请日:1994-11-18
Applicant: TEXACO DEVELOPMENT CORP
Inventor: BROOKER DUANE D , FALSETTI JAMES S , WOLFENBARGER JAMES K , VUONG DINH-CUONG
IPC: F23J1/02 , B01J7/00 , C10J3/00 , C10J3/20 , C10J3/48 , C10J3/72 , C10J3/76 , C10K1/00 , F23G5/12 , F23J1/08 , C10J3/68
Abstract: A gasifier for partially combusting a carbonaceous fuel mixture in the combustion chamber of the gasifier. The latter includes a water bath into which the hot effluent or products of combustion are immersed, including a synthetic gas. The products of combustion are directed into the bath by way of a constricted throat section. To avoid excessive erosion action and/or thermal shock to the throat section as a result of exposure to the effluent's high temperatures, the throat section is structured with an internal framework of pipes. The framework is communicated with a pressurized source of a cooling fluid, preferably water, whereby to cool the throat section sufficiently to counteract the ill effects of exposure to contact with the high temperature effluent.
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公开(公告)号:BR9408116A
公开(公告)日:1997-08-05
申请号:BR9408116
申请日:1994-11-18
Applicant: TEXACO DEVELOPMENT CORP
Inventor: VUONG DINH-CUONG
Abstract: An evaporator, which includes a water chamber for receiving water to be evaporated. A plurality of evaporator tubes which when heated, and when water is on an inner wall of a tube, evaporates at least a portion of that water. A plurality of distributors spatially connecting the water chamber with the evaporator tubes in a manner so that each distributor uniformly and distributes the water from the water chamber to an inner wall of a corresponding evaporator tube. A heat source, which heats the plurality of tubes to an evaporation temperature. Apparatus distills the water vapor resulting from the water evaporation to provide distilled water.
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公开(公告)号:CA2154954A1
公开(公告)日:1996-02-16
申请号:CA2154954
申请日:1995-06-28
Applicant: TEXACO DEVELOPMENT CORP
Inventor: VUONG DINH-CUONG , BROOKER DONALD DUANE , FALSETTI JAMES SAMUEL , WOLFENBARGER JAMES KENNETH
IPC: B01J19/00 , C01B3/36 , C10J3/00 , C10J3/46 , C10J3/48 , C10L1/00 , F23J1/00 , F27D3/00 , C10J3/08 , C01B3/32
Abstract: A selective deslagging operation is conducted in a partial oxidation reactor wherein a first predetermined portion of the reactor is selectively deslagged by derivatization while limiting derivatizing slag conditions in a second predetermined portion of the reactor. Selective deslagging can be accomplished by controlled oxidation conditions in the reactor that vary from one predetermined portion of the reactor to another. Thus, the slag present in one predetermined portion is derivatized and fluidized for removal from the reactor at a faster rate than the slag present in another portion of the reactor, which is not derivatized or is subjected to more limited derivatizing slag conditions. Derivatized slag can be differentiated from non-derivatized slag that does not flow or more limited derivatized slag that has a lower mass flow rate then the derivatized slag at conditions of controlled oxidation. The derivatized slag can then be selectively removed because it has attained a lower fluidizing temperature.
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