CN1156402C - 气液连续反应的方法和装置 - Google Patents
气液连续反应的方法和装置 Download PDFInfo
- Publication number
- CN1156402C CN1156402C CNB998165735A CN99816573A CN1156402C CN 1156402 C CN1156402 C CN 1156402C CN B998165735 A CNB998165735 A CN B998165735A CN 99816573 A CN99816573 A CN 99816573A CN 1156402 C CN1156402 C CN 1156402C
- Authority
- CN
- China
- Prior art keywords
- liquid
- gas
- reactor
- chamber
- chambers
- Prior art date
- Legal status (The legal status 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 status listed.)
- Expired - Fee Related
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F11/00—Compounds of calcium, strontium, or barium
- C01F11/18—Carbonates
- C01F11/181—Preparation of calcium carbonate by carbonation of aqueous solutions and characterised by control of the carbonation conditions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J10/00—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/245—Stationary reactors without moving elements inside placed in series
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00716—Means for reactor start-up
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00761—Details of the reactor
- B01J2219/00763—Baffles
- B01J2219/00765—Baffles attached to the reactor wall
- B01J2219/00768—Baffles attached to the reactor wall vertical
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/18—Details relating to the spatial orientation of the reactor
- B01J2219/182—Details relating to the spatial orientation of the reactor horizontal
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
Description
实际的实验条件 | ||
运行数 | - | 4 |
气体温度 | °F(℃) | 68.00(20) |
气体基准压力 | psig | 0.00 |
气体总流量 | cfm(Lm) | 60.00(1699) |
CO2气体的浓度 | vol% | 15.00 |
CO2流量 | cfm(Lm) | 9.02(255.4) |
CO2流量 | lb/min(g/min) | 1.03(466) |
气体效率 | % | 51.58 |
PCC率 | lb/min(g/min) | 1.21(548) |
PCC率 | lb/h(kg/h) | 72.45(32.82) |
平均熟化MO | ml-1N-HCl | 7.90 |
熟化进料率(Slake Feedrate) | gpm | 1.83 |
SSA | m2/g | 4.40 |
产品形态 | - | 文石 |
反应器总容积 | gal(L) | 122.55(463.88) |
区域数 | - | 14.00 |
区域体积,区域1-4 | gal/zone(L/zone) | 3.68(13.92) |
区域体积,区域5-13 | gal/zone(L/zone) | 10.17(38.49) |
区域体积,区域14 | gal/zone(L/zone) | 16.31(61.73) |
Claims (21)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/293,614 | 1999-04-16 | ||
US09/293,614 US6451268B1 (en) | 1999-04-16 | 1999-04-16 | Method and apparatus for continuous gas liquid reactions |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1348429A CN1348429A (zh) | 2002-05-08 |
CN1156402C true CN1156402C (zh) | 2004-07-07 |
Family
ID=23129797
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNB998165735A Expired - Fee Related CN1156402C (zh) | 1999-04-16 | 1999-12-22 | 气液连续反应的方法和装置 |
Country Status (17)
Country | Link |
---|---|
US (2) | US6451268B1 (zh) |
EP (1) | EP1189840B1 (zh) |
JP (1) | JP2002542023A (zh) |
KR (1) | KR20020003234A (zh) |
CN (1) | CN1156402C (zh) |
AT (1) | ATE330907T1 (zh) |
AU (1) | AU2819900A (zh) |
BR (1) | BR9917260A (zh) |
CA (1) | CA2367372C (zh) |
DE (1) | DE69932101T2 (zh) |
HK (1) | HK1046525B (zh) |
IL (2) | IL145604A (zh) |
PL (1) | PL197473B1 (zh) |
PT (1) | PT1189840E (zh) |
RU (1) | RU2232717C2 (zh) |
SK (1) | SK286324B6 (zh) |
WO (1) | WO2000063118A1 (zh) |
Families Citing this family (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6726187B2 (en) * | 2001-10-30 | 2004-04-27 | Hydrogenics Corporation | Humidifier |
SE524540C2 (sv) * | 2002-11-18 | 2004-08-24 | Alfa Laval Corp Ab | Flödesstyrande insats i en reaktorkammare samt reaktor försedd med insatsen |
CA2467469C (en) * | 2004-05-17 | 2007-02-13 | 665187 Alberta Ltd. | Sewage containment system |
FI120032B (fi) * | 2004-07-13 | 2009-06-15 | Fp Pigments Oy | Menetelmä ja laite kalsiumkarbonaattituotteen valmistamiseksi, tuote ja sen käyttö |
FR2876375B1 (fr) * | 2004-10-12 | 2007-02-02 | Arkema Sa | Procede de preparation d'esters ou d'anydrides (meth) acryliques |
EP1746073A1 (en) * | 2005-07-20 | 2007-01-24 | SOLVAY (Société Anonyme) | Process for making a solid compound by precipitation, suspensions of solid in liquids and solids obtained by the process and their use as additives |
US8038959B2 (en) * | 2005-09-08 | 2011-10-18 | Casio Computer Co., Ltd. | Reacting device |
US7572417B2 (en) * | 2005-09-29 | 2009-08-11 | Casio Computer Co., Ltd. | Reactor |
JP4665803B2 (ja) * | 2006-03-14 | 2011-04-06 | カシオ計算機株式会社 | 反応装置 |
BRPI0601717A (pt) * | 2006-05-04 | 2007-12-18 | Du Pont Brasil | processo para a fabricação de carbonato de cálcio |
CN101553430A (zh) * | 2006-08-29 | 2009-10-07 | 耶德研究和发展有限公司 | 用于降低流体的co2浓度的方法和设备 |
PL2144851T3 (pl) * | 2007-04-20 | 2016-10-31 | Sposób wytwarzania pcc | |
CA2786099A1 (en) | 2011-12-07 | 2013-03-15 | Tracy Peter Aberle | System and apparatus for evacuation of contaminated fluids from flexible hulled vessels |
RU2497567C1 (ru) * | 2012-06-06 | 2013-11-10 | ОТКРЫТОЕ АКЦИОНЕРНОЕ ОБЩЕСТВО "СИБУР Холдинг" | Газожидкостный реактор |
BR112017007039B8 (pt) * | 2014-10-07 | 2022-09-13 | N & U As | Reator para hidrólise enzimática de um material. |
US10752530B1 (en) * | 2015-09-22 | 2020-08-25 | James Dartez | Submersible aerator and mixing apparatus |
BR112018014966B1 (pt) | 2016-01-21 | 2022-11-29 | Squaretail Pty Ltd | Método e aparelho para a remoção do dióxido de carbono a partir do gás de combustão |
KR102567914B1 (ko) * | 2018-06-19 | 2023-08-17 | 고등기술연구원연구조합 | 격벽식 이산화탄소 광물화 반응기 |
US11214489B1 (en) * | 2020-11-28 | 2022-01-04 | Ceres Technology, LLC | Crossflow scrubbing method and apparatus to produce a product such as potassium thiosulfate or ammonium thiosulfate |
KR102503821B1 (ko) * | 2022-02-09 | 2023-02-23 | 현대오일뱅크 주식회사 | 반건식 탄산화 방법 |
Family Cites Families (45)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2000953A (en) | 1933-10-30 | 1935-05-14 | Hooker Electrochemical Co | Means for reacting semifluid materials |
US2538802A (en) | 1947-05-03 | 1951-01-23 | Ecusta Paper Corp | Method of manufacturing calcium carbonate |
US2704206A (en) | 1954-01-21 | 1955-03-15 | Crook Isadore | Mixing and dispensing device |
US3045984A (en) | 1959-06-08 | 1962-07-24 | Fredric E Cochran | Fluid blender |
US3150926A (en) | 1961-05-15 | 1964-09-29 | Champion Papers Inc | Fluidized production of calcium carbonate |
CH419062A (de) * | 1962-09-17 | 1966-08-31 | Forsch Inst Prof Ing Chem P Wi | Verfahren zur physikalischen und/oder chemischen Behandlung von Stoffen sowie Vorrichtung zum Durchführen des Verfahrens |
GB1173302A (en) | 1966-07-20 | 1969-12-10 | Rolls Royce | Mixing Device and Mixing Method for Fluids |
US3856270A (en) | 1973-10-09 | 1974-12-24 | Fmc Corp | Static fluid mixing apparatus |
US3920800A (en) * | 1973-10-12 | 1975-11-18 | Cyprus Mines Corp | Production of purified calcium carbonate |
JPS5339998A (en) | 1976-09-25 | 1978-04-12 | Shiraishi Kogyo Kaisha Ltd | Process for contnuously preparing precipitated calcium carbonate |
FR2385739A1 (fr) * | 1977-03-30 | 1978-10-27 | Poudres & Explosifs Ste Nale | Nouveau procede de nitration en continu de la cellulose et installation pour la mise en oeuvre d'un tel procede |
US4313680A (en) | 1979-11-05 | 1982-02-02 | Chevron Research Company | Reactor for fast reactions |
US4432914A (en) * | 1982-06-23 | 1984-02-21 | Kenneth C. Schifftner, Inc. | Mass transfer contact apparatus |
NL8303350A (nl) | 1982-11-06 | 1984-06-01 | Kernforschungsz Karlsruhe | Statische menger. |
US4518544A (en) * | 1983-01-20 | 1985-05-21 | Baltimore Aircoil Company, Inc. | Serpentine film fill packing for evaporative heat and mass exchange |
JPS61242636A (ja) * | 1985-03-29 | 1986-10-28 | Hitachi Ltd | 反応装置 |
US4702893A (en) * | 1985-06-27 | 1987-10-27 | Kirk Samuel A | Acid air pollution precipitators |
US4888160A (en) | 1985-12-20 | 1989-12-19 | J.M. Huber Corporation | Process for producing calcium carbonate and products thereof |
US5133941A (en) * | 1988-08-19 | 1992-07-28 | Phillips Petroleum Company | Apparatus for hydrogenating hydrocarbons |
US5352421A (en) | 1989-12-05 | 1994-10-04 | University Of Toronto Innovations Foundation | Method and apparatus for effecting gas-liquid contact |
US5382271A (en) * | 1991-12-26 | 1995-01-17 | Industrial Technology Research Institute | Hydrogen generator |
JPH05261389A (ja) * | 1992-03-17 | 1993-10-12 | Hitachi Plant Eng & Constr Co Ltd | 多段廃水処理槽 |
JPH06221633A (ja) | 1993-01-26 | 1994-08-12 | Toshiba Corp | 換気口のカバー装置 |
JPH06285364A (ja) | 1993-04-07 | 1994-10-11 | Chiyoda Corp | 循環流動接触反応方法及びその装置 |
US6258993B1 (en) * | 1993-09-29 | 2001-07-10 | Regents Of The University Of Minnesota | Simulated countercurrent moving bed chromatographic reactor and method for use thereof |
MY116340A (en) * | 1993-12-15 | 2004-01-31 | Chiyoda Corp | Liquid flow control device, reactor using same and liquid flow control method |
CA2141886E (en) * | 1994-05-11 | 1999-10-12 | Federico Zardi | Reactor for two-phase reactions, in particular for urea synthesis at high pressure and temperature |
JPH07308569A (ja) | 1994-05-17 | 1995-11-28 | Idemitsu Kosan Co Ltd | 気泡塔 |
US5658537A (en) * | 1995-07-18 | 1997-08-19 | Basf Corporation | Plate-type chemical reactor |
SI9500237B (sl) * | 1995-07-26 | 2003-12-31 | Omya Gmbh. | Naprava za kontinuirno proizvodnjo obarjenega kalcijevega karbonata |
US5846500A (en) * | 1995-10-10 | 1998-12-08 | James W. Bunger And Associates, Inc. | Process for purifying highly impure calcium hydroxide and for producing high-value precipitated calcium carbonate and other calcium products |
US5766519A (en) * | 1995-11-13 | 1998-06-16 | Erickson; Donald C. | Locally cocurrent globally crosscurrent pressure equalized absorber and process |
RU2114691C1 (ru) | 1995-11-20 | 1998-07-10 | Товарищество с ограниченной ответственностью "Экос" | Реактор |
US5779464A (en) * | 1996-01-10 | 1998-07-14 | The Ohio State University Research Foundation | Calcium carbonate sorbent and methods of making and using same |
AT403043B (de) | 1996-04-03 | 1997-10-27 | Unitechnik Thurner Anlagenbaug | Verfahren zur kontinuierlichen erzeugung von gefälltem kalziumkarbonat |
ID19133A (id) * | 1996-12-12 | 1998-06-18 | Praxair Technology Inc | Pengisian oksigen langsung kedalam reaktor-reaktor ruang gelembung |
JPH10174862A (ja) | 1996-12-17 | 1998-06-30 | Hitachi Ltd | 連続反応装置 |
JP3066462B2 (ja) | 1997-03-17 | 2000-07-17 | 工業技術院長 | 気液接触装置 |
US5876679A (en) * | 1997-04-08 | 1999-03-02 | Dorr-Oliver, Inc. | Fluid bed reactor |
AT405277B (de) * | 1997-07-07 | 1999-06-25 | Unitechnik Thurner Anlagenbaug | Vorrichtung zur, insbesondere kontinuierlichen, herstellung von caco3 in dispergierter form |
JP3268246B2 (ja) | 1997-11-07 | 2002-03-25 | エア・ウォーター株式会社 | 気液接触方法および装置 |
JPH11188255A (ja) | 1997-12-25 | 1999-07-13 | Takaoka Electric Mfg Co Ltd | 気液混合槽 |
US6080372A (en) * | 1998-09-11 | 2000-06-27 | Air Products And Chemicals, Inc. | Two stage reactor for continuous three phase slurry hydrogenation and method of operation |
JP2000249464A (ja) | 1998-12-28 | 2000-09-14 | Nippon Sanso Corp | 気液接触装置、空気液化分離装置、およびガス分離方法 |
JP4558868B2 (ja) | 1999-11-05 | 2010-10-06 | 株式会社ニクニ | 気液混合溶解装置 |
-
1999
- 1999-04-16 US US09/293,614 patent/US6451268B1/en not_active Expired - Lifetime
- 1999-12-22 WO PCT/IB1999/002118 patent/WO2000063118A1/en active IP Right Grant
- 1999-12-22 SK SK1414-2001A patent/SK286324B6/sk not_active IP Right Cessation
- 1999-12-22 AT AT99969242T patent/ATE330907T1/de not_active IP Right Cessation
- 1999-12-22 CN CNB998165735A patent/CN1156402C/zh not_active Expired - Fee Related
- 1999-12-22 RU RU2001130902/15A patent/RU2232717C2/ru not_active IP Right Cessation
- 1999-12-22 BR BR9917260-7A patent/BR9917260A/pt not_active IP Right Cessation
- 1999-12-22 CA CA002367372A patent/CA2367372C/en not_active Expired - Fee Related
- 1999-12-22 KR KR1020017013020A patent/KR20020003234A/ko active IP Right Grant
- 1999-12-22 IL IL14560499A patent/IL145604A/xx not_active IP Right Cessation
- 1999-12-22 PL PL365816A patent/PL197473B1/pl not_active IP Right Cessation
- 1999-12-22 JP JP2000612219A patent/JP2002542023A/ja active Pending
- 1999-12-22 PT PT99969242T patent/PT1189840E/pt unknown
- 1999-12-22 EP EP99969242A patent/EP1189840B1/en not_active Expired - Lifetime
- 1999-12-22 AU AU28199/00A patent/AU2819900A/en not_active Abandoned
- 1999-12-22 DE DE69932101T patent/DE69932101T2/de not_active Expired - Lifetime
-
2002
- 2002-05-08 US US10/141,564 patent/US7387769B2/en not_active Expired - Fee Related
- 2002-11-06 HK HK02108050.8A patent/HK1046525B/zh not_active IP Right Cessation
-
2005
- 2005-02-03 IL IL16667305A patent/IL166673A0/xx unknown
Also Published As
Publication number | Publication date |
---|---|
IL166673A0 (en) | 2006-01-15 |
DE69932101T2 (de) | 2007-06-21 |
JP2002542023A (ja) | 2002-12-10 |
PT1189840E (pt) | 2006-11-30 |
IL145604A0 (en) | 2002-06-30 |
ATE330907T1 (de) | 2006-07-15 |
DE69932101D1 (de) | 2006-08-03 |
US7387769B2 (en) | 2008-06-17 |
HK1046525A1 (en) | 2003-01-17 |
PL197473B1 (pl) | 2008-04-30 |
SK286324B6 (en) | 2008-07-07 |
EP1189840A1 (en) | 2002-03-27 |
CA2367372C (en) | 2008-08-05 |
HK1046525B (zh) | 2005-04-08 |
EP1189840B1 (en) | 2006-06-21 |
WO2000063118A1 (en) | 2000-10-26 |
AU2819900A (en) | 2000-11-02 |
KR20020003234A (ko) | 2002-01-10 |
BR9917260A (pt) | 2002-01-08 |
US6451268B1 (en) | 2002-09-17 |
US20020176813A1 (en) | 2002-11-28 |
PL365816A1 (en) | 2005-01-10 |
RU2232717C2 (ru) | 2004-07-20 |
IL145604A (en) | 2005-06-19 |
CN1348429A (zh) | 2002-05-08 |
CA2367372A1 (en) | 2000-10-26 |
SK14142001A3 (sk) | 2002-09-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN1156402C (zh) | 气液连续反应的方法和装置 | |
CN1157329C (zh) | 硝酸的生产方法 | |
US6984323B2 (en) | Biological treatment process | |
US6478963B1 (en) | Method and device for anaerobic purification of waste water using the UASB method | |
EP0820574B1 (en) | A method of producing gas hydrate | |
AU2008279963C1 (en) | Plant for aerobic and anaerobic digestion treatment by PFR | |
CN1087966C (zh) | 含二氧化硫废气的脱硫方法 | |
CN1116131A (zh) | 带有用于烟道气湿法脱硫的气体多层筛板的方法和装置 | |
US4017592A (en) | Process for production of aqueous hypochlorous acid solution | |
JPWO2005039746A1 (ja) | 散気処理装置 | |
CN1222354C (zh) | 氨基甲酸盐冷凝设备 | |
AU740348B2 (en) | Biochemical oxidation system and process | |
CN1787982A (zh) | 从气态反应物中制备液态产品以及任选的气态产品的方法 | |
CN1141248C (zh) | 带有空气喷射器的亚硫酸发生器 | |
CN1192723A (zh) | 包括经过冷却除结晶硫步骤的处理含硫化氢的气体的方法和装置 | |
CN1547558A (zh) | 厌氧处理装置 | |
CN1823015A (zh) | 含硫化合物废水的厌氧处理方法和设备 | |
CN108147534A (zh) | 硝化反硝化一体化生物反应器 | |
CN1966139A (zh) | 双环流复合式反应装置 | |
CN1840523A (zh) | 尿素制备方法及相关设备 | |
JP2016531728A (ja) | 水溶液から硫化物を除去するためのプロセス | |
CN1013360B (zh) | 有机基质的厌氧分解法及其设备 | |
CN221296467U (zh) | 圆柱形潜流式abr厌氧反应器 | |
CN1029834C (zh) | 废水处理的方法 | |
CN112481072B (zh) | 一种柠檬酸发酵系统及工艺 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
REG | Reference to a national code |
Ref country code: HK Ref legal event code: GR Ref document number: 1046525 Country of ref document: HK |
|
ASS | Succession or assignment of patent right |
Owner name: MICHIGAN SPECIAL ORE COMPANY Free format text: FORMER OWNER: MINERALS TECH INC. Effective date: 20090918 |
|
C41 | Transfer of patent application or patent right or utility model | ||
TR01 | Transfer of patent right |
Effective date of registration: 20090918 Address after: Michigan Patentee after: Specialty Michigan Minerals, Inc. Address before: American New York Patentee before: Mining Industry Tech. Co., Ltd. |
|
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20040707 Termination date: 20171222 |
|
CF01 | Termination of patent right due to non-payment of annual fee |