DD150006A5 - Chemisches verfahren und reaktionsgefaess fuer die durchfuehrung desselben - Google Patents
Chemisches verfahren und reaktionsgefaess fuer die durchfuehrung desselben Download PDFInfo
- Publication number
- DD150006A5 DD150006A5 DD80220171A DD22017180A DD150006A5 DD 150006 A5 DD150006 A5 DD 150006A5 DD 80220171 A DD80220171 A DD 80220171A DD 22017180 A DD22017180 A DD 22017180A DD 150006 A5 DD150006 A5 DD 150006A5
- Authority
- DD
- German Democratic Republic
- Prior art keywords
- catalyst
- gas
- catalyst layer
- reaction
- reaction vessel
- Prior art date
Links
- 238000001311 chemical methods and process Methods 0.000 title 1
- 239000003054 catalyst Substances 0.000 claims abstract description 212
- 238000006243 chemical reaction Methods 0.000 claims abstract description 160
- 238000001816 cooling Methods 0.000 claims abstract description 75
- 238000000034 method Methods 0.000 claims abstract description 67
- 239000002826 coolant Substances 0.000 claims abstract description 41
- 238000009826 distribution Methods 0.000 claims abstract description 25
- 239000007858 starting material Substances 0.000 claims abstract description 20
- 239000011949 solid catalyst Substances 0.000 claims abstract description 5
- 239000007789 gas Substances 0.000 claims description 131
- 239000003507 refrigerant Substances 0.000 claims description 29
- 230000002093 peripheral effect Effects 0.000 claims description 25
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 18
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 230000003197 catalytic effect Effects 0.000 claims description 10
- 229910021529 ammonia Inorganic materials 0.000 claims description 9
- 238000009835 boiling Methods 0.000 claims description 9
- 239000001257 hydrogen Substances 0.000 claims description 7
- 229910052739 hydrogen Inorganic materials 0.000 claims description 7
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 6
- 238000010574 gas phase reaction Methods 0.000 claims description 6
- 238000012856 packing Methods 0.000 claims description 6
- 238000005192 partition Methods 0.000 claims description 5
- 239000002574 poison Substances 0.000 claims description 5
- 231100000614 poison Toxicity 0.000 claims description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 3
- 239000000969 carrier Substances 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 239000007791 liquid phase Substances 0.000 claims 4
- 241000282320 Panthera leo Species 0.000 claims 1
- 239000002243 precursor Substances 0.000 claims 1
- 230000008569 process Effects 0.000 abstract description 10
- 239000007788 liquid Substances 0.000 description 34
- 239000000203 mixture Substances 0.000 description 14
- 238000012546 transfer Methods 0.000 description 14
- 238000004519 manufacturing process Methods 0.000 description 12
- 239000000463 material Substances 0.000 description 11
- 239000004215 Carbon black (E152) Substances 0.000 description 9
- 230000000694 effects Effects 0.000 description 9
- 229930195733 hydrocarbon Natural products 0.000 description 9
- 150000002430 hydrocarbons Chemical class 0.000 description 9
- 239000000126 substance Substances 0.000 description 8
- 239000000110 cooling liquid Substances 0.000 description 7
- 238000009834 vaporization Methods 0.000 description 7
- 230000008016 vaporization Effects 0.000 description 7
- 230000008901 benefit Effects 0.000 description 6
- 230000008646 thermal stress Effects 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 230000008859 change Effects 0.000 description 4
- 238000010276 construction Methods 0.000 description 4
- 239000012084 conversion product Substances 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 238000001704 evaporation Methods 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 230000009467 reduction Effects 0.000 description 4
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000007086 side reaction Methods 0.000 description 3
- 238000003466 welding Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 2
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 150000008280 chlorinated hydrocarbons Chemical class 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- NEHMKBQYUWJMIP-UHFFFAOYSA-N chloromethane Chemical compound ClC NEHMKBQYUWJMIP-UHFFFAOYSA-N 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- XLJMAIOERFSOGZ-UHFFFAOYSA-N cyanic acid Chemical compound OC#N XLJMAIOERFSOGZ-UHFFFAOYSA-N 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- JMANVNJQNLATNU-UHFFFAOYSA-N glycolonitrile Natural products N#CC#N JMANVNJQNLATNU-UHFFFAOYSA-N 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 230000002035 prolonged effect Effects 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 229930195734 saturated hydrocarbon Natural products 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 229930195735 unsaturated hydrocarbon Natural products 0.000 description 2
- MHCVCKDNQYMGEX-UHFFFAOYSA-N 1,1'-biphenyl;phenoxybenzene Chemical compound C1=CC=CC=C1C1=CC=CC=C1.C=1C=CC=CC=1OC1=CC=CC=C1 MHCVCKDNQYMGEX-UHFFFAOYSA-N 0.000 description 1
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- -1 Cyanogen compound Chemical class 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- NHTMVDHEPJAVLT-UHFFFAOYSA-N Isooctane Chemical compound CC(C)CC(C)(C)C NHTMVDHEPJAVLT-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- LGRFSURHDFAFJT-UHFFFAOYSA-N Phthalic anhydride Natural products C1=CC=C2C(=O)OC(=O)C2=C1 LGRFSURHDFAFJT-UHFFFAOYSA-N 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 1
- 238000005804 alkylation reaction Methods 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- JHIWVOJDXOSYLW-UHFFFAOYSA-N butyl 2,2-difluorocyclopropane-1-carboxylate Chemical compound CCCCOC(=O)C1CC1(F)F JHIWVOJDXOSYLW-UHFFFAOYSA-N 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000012809 cooling fluid Substances 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- JVSWJIKNEAIKJW-UHFFFAOYSA-N dimethyl-hexane Natural products CCCCCC(C)C JVSWJIKNEAIKJW-UHFFFAOYSA-N 0.000 description 1
- USIUVYZYUHIAEV-UHFFFAOYSA-N diphenyl ether Chemical class C=1C=CC=CC=1OC1=CC=CC=C1 USIUVYZYUHIAEV-UHFFFAOYSA-N 0.000 description 1
- 210000004907 gland Anatomy 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000003449 preventive effect Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 230000035882 stress Effects 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Classifications
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/0005—Catalytic processes under superatmospheric pressure
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/0207—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal
- B01J8/0214—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal in a cylindrical annular shaped bed
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/0285—Heating or cooling the reactor
-
- 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
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
- B01J2208/00132—Tubes
-
- 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
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
- B01J2208/00194—Tubes
-
- 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
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00884—Means for supporting the bed of particles, e.g. grids, bars, perforated plates
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP54039306A JPS5839572B2 (ja) | 1979-04-03 | 1979-04-03 | 反応器およびその使用法 |
Publications (1)
Publication Number | Publication Date |
---|---|
DD150006A5 true DD150006A5 (de) | 1981-08-12 |
Family
ID=12549423
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DD80220171A DD150006A5 (de) | 1979-04-03 | 1980-04-02 | Chemisches verfahren und reaktionsgefaess fuer die durchfuehrung desselben |
Country Status (18)
Families Citing this family (72)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0080270B1 (en) * | 1981-11-19 | 1985-09-04 | Imperial Chemical Industries Plc | Synthesis process and reactor |
DE3275066D1 (en) * | 1981-12-14 | 1987-02-19 | Ici Plc | Chemical reactor and process |
EP0081948B1 (en) * | 1981-12-14 | 1987-05-13 | Imperial Chemical Industries Plc | Reactor |
DE3217066A1 (de) * | 1982-05-06 | 1983-11-10 | Linde Ag, 6200 Wiesbaden | Reaktor zur durchfuehrung katalytischer reaktion |
JPS5959242A (ja) * | 1982-09-28 | 1984-04-05 | Toyo Eng Corp | 反応方法およびそのための反応器 |
US4554135A (en) * | 1982-11-26 | 1985-11-19 | C F Braun & Co. | Ammonia converter |
JPS59162942A (ja) * | 1983-03-07 | 1984-09-13 | Toyo Eng Corp | 反応器 |
DE3318098A1 (de) * | 1983-05-18 | 1984-11-22 | Linde Ag, 6200 Wiesbaden | Verfahren und reaktor zur durchfuehrung einer endo- oder exothermen reaktion |
JPS6031824A (ja) * | 1983-07-29 | 1985-02-18 | Mitsui Eng & Shipbuild Co Ltd | 触媒反応塔 |
JPS60106527A (ja) * | 1983-11-14 | 1985-06-12 | Mitsubishi Heavy Ind Ltd | 二重管式発熱反応器 |
JPS60122036A (ja) * | 1983-12-05 | 1985-06-29 | Mitsubishi Heavy Ind Ltd | 触媒充填反応器 |
JPS60150824A (ja) * | 1984-01-18 | 1985-08-08 | Toyo Eng Corp | 改良反応器 |
US4743432A (en) * | 1984-11-16 | 1988-05-10 | M.A.N. Maschinenfabrik Augsburg-Nurnberg | Vertical reactor for the generation of methanol |
JPS6274447A (ja) * | 1985-09-27 | 1987-04-06 | エムア−エン・グ−テホツフヌングスヒユツテ・ゲゼルシヤフト・ミツト・ベシユレンクテル・ハフトウング | 触媒発熱反応および吸熱反応用縦形反応器 |
DE3605792A1 (de) * | 1985-09-27 | 1987-04-02 | Gutehoffnungshuette Man | Stehender reaktor fuer katalytische exotherme und endotherme reaktionen, insbesondere zur herstellung von methanol, ammoniak, synthesegas und hoeheren alkoholen |
FI75100C (sv) * | 1986-03-03 | 1988-05-09 | Rm Metal Consulting Ky | Katalysatorbädd för exoterma reaktioner mellan gaser eller vätskor. |
CA1296023C (en) * | 1986-07-24 | 1992-02-18 | Maarten Johannes Van Der Burgt | Process for converting a gaseous feed into an at least partly liquidproduct |
GB8627897D0 (en) * | 1986-11-21 | 1986-12-31 | Shell Int Research | Reactor |
US4880604A (en) * | 1987-11-04 | 1989-11-14 | Uop | Apparatus for coke burning in regeneration of hydrocarbon conversion catalyst |
FR2625112B1 (fr) * | 1987-12-23 | 1993-10-22 | Institut Francais Petrole | Reacteur a controle thermique interne par plaques creuses echangeuses de chaleur |
DK167242B1 (da) * | 1989-02-16 | 1993-09-27 | Topsoe Haldor As | Apparat og fremgangsmaade til exoterme reaktioner |
JP2547278B2 (ja) * | 1990-11-16 | 1996-10-23 | 東洋エンジニアリング株式会社 | 反応器 |
DE4131446A1 (de) * | 1991-09-21 | 1993-06-09 | Basf Ag, 6700 Ludwigshafen, De | Reaktor und verfahren zur durchfuehrung heterogenkatalytischer gasphasenreaktionen |
US5869011A (en) * | 1994-02-01 | 1999-02-09 | Lee; Jing Ming | Fixed-bed catalytic reactor |
US5520891A (en) * | 1994-02-01 | 1996-05-28 | Lee; Jing M. | Cross-flow, fixed-bed catalytic reactor |
US5676911A (en) * | 1995-12-14 | 1997-10-14 | Her Majesty The Queen In Right Of Canada, As Represented By The Minister Of National Defence Of Her Majesty's Canadian Government | Radial flow fuel processor |
US6955793B1 (en) * | 1997-06-18 | 2005-10-18 | Arencibia Jr Jose P | Temperature controlled reaction vessel |
US5989500A (en) * | 1997-07-02 | 1999-11-23 | Phillips Petroleum Company | Reactor heat exchange system |
RU2234975C2 (ru) | 1998-07-09 | 2004-08-27 | Стоун энд Вебстэ, Инк. | Проточный реактор с радиальным потоком и способ обработки жидкого потока реагентов |
US6171570B1 (en) * | 1998-10-12 | 2001-01-09 | Kellogg Brown & Root, Inc. | Isothermal ammonia converter |
GB0106308D0 (en) * | 2001-03-14 | 2001-05-02 | Kvaerner Process Tech Ltd | Apparatus |
GB0113078D0 (en) * | 2001-05-30 | 2001-07-18 | Kvaerner Process Tech Ltd | Process and plant |
GB0115243D0 (en) * | 2001-06-21 | 2001-08-15 | Kvaerner Process Tech Ltd | Method |
RU2181622C1 (ru) * | 2001-11-29 | 2002-04-27 | Закрытое акционерное общество "Метанол" | Установка для гомогенного окисления природного газа и способ гомогенного окисления природного газа |
RU2199366C1 (ru) * | 2002-01-11 | 2003-02-27 | Закрытое акционерное общество "Метанол" | Реактор для гомогенного окисления природного газа |
EP1376040A1 (en) * | 2002-06-28 | 2004-01-02 | Methanol Casale S.A. | Multiservice heat exchange unit |
US7081230B2 (en) * | 2002-11-15 | 2006-07-25 | Kellogg Brown & Root Llc | Split-flow, vertical ammonia converter |
WO2006045457A1 (en) * | 2004-10-26 | 2006-05-04 | Haldor Topsøe A/S | Reactor and process for carrying out endothermic or exothermic catalytic reactions |
DE102006011496A1 (de) * | 2006-03-14 | 2007-09-20 | Bayer Technology Services Gmbh | Verfahren und Vorrichtung zur Herstellung von Chlor durch Gasphasenoxidation in einem gekühlten Wandreaktor |
FR2900066B1 (fr) * | 2006-04-21 | 2008-05-30 | Inst Francais Du Petrole | Nouvel echangeur interne pour reacteur en lit fluidise gaz liquide solide, mettant en oeuvre une reaction fortement exothermique. |
EP1930679B1 (de) * | 2006-12-01 | 2009-07-15 | Basf Se | Verfahren und Vorrichtung zur Kühlung von Reaktoren mit siedenden Flüssigkeiten |
DE202007006812U1 (de) * | 2007-05-11 | 2008-09-18 | Man Dwe Gmbh | Kühlrohrreaktor |
EP2075057A1 (en) * | 2007-12-21 | 2009-07-01 | Methanol Casale S.A. | Radial isothermal chemical reactor |
DE102008023042A1 (de) * | 2008-05-09 | 2009-11-12 | Süd-Chemie AG | Verfahren zur semi-adiabatischen, semi-isothermen Durchführung einer endothermen Reaktion unter Einsatz eines katalytischen Reaktors und Ausbildung dieses Reaktors |
FR2948580B1 (fr) * | 2009-07-29 | 2011-07-22 | Inst Francais Du Petrole | Dispositif de distribution de la charge et de recuperation des effluents dans un reacteur catalytique a lit radial |
KR101842056B1 (ko) * | 2010-02-04 | 2018-03-26 | 할도르 토프쉐 에이/에스 | 디메틸 에테르의 제조 방법 |
GB201107072D0 (en) * | 2011-04-27 | 2011-06-08 | Davy Process Techn Ltd | Process |
DE102012220930A1 (de) | 2012-11-15 | 2014-05-15 | Chemieanlagenbau Chemnitz Gmbh | Festbettreaktor |
DE102012220926A1 (de) * | 2012-11-15 | 2014-05-15 | Chemieanlagenbau Chemnitz Gmbh | Festbettreaktor |
CN103990420A (zh) * | 2013-02-20 | 2014-08-20 | 上海融熠投资管理有限公司 | 列管式固定床反应器及其应用 |
CN103435006B (zh) * | 2013-08-20 | 2015-04-08 | 湖南安淳高新技术有限公司 | 一种高co高变换率等温变换反应器及其工艺 |
EP2933016A1 (en) * | 2014-04-18 | 2015-10-21 | Casale Sa | Isothermal tubular catalytic reactor |
CN104048530B (zh) * | 2014-06-24 | 2016-04-20 | 中建材(合肥)粉体科技装备有限公司 | 弯道缓流式粉体冷却器 |
CN104841340A (zh) * | 2015-05-19 | 2015-08-19 | 中国五环工程有限公司 | 一种用于合成气制乙二醇工艺的新型羰化反应器 |
WO2017019961A1 (en) * | 2015-07-29 | 2017-02-02 | Primus Green Energy Inc. | Two-stage reactor for exothermal and reversible reactions and methods thereof |
DE102015214943A1 (de) | 2015-08-05 | 2017-02-09 | Siemens Aktiengesellschaft | Verfahren und Anlage für eine chemische Synthese |
CN105032305B (zh) * | 2015-08-27 | 2017-10-20 | 德艾柯工程技术(上海)有限公司 | 一种新型径向板式反应器 |
GB201600793D0 (en) | 2016-01-15 | 2016-03-02 | Johnson Matthey Davy Technologies Ltd | Methanol process |
GB201600794D0 (en) | 2016-01-15 | 2016-03-02 | Johnson Matthey Davy Technologies Ltd | Methanol process |
CN108854861A (zh) * | 2017-05-09 | 2018-11-23 | 德艾柯工程技术(上海)有限公司 | 一种模块化控温反应器 |
KR102070704B1 (ko) | 2018-01-08 | 2020-01-29 | 에스케이실트론 주식회사 | 슬러리 냉각장치 및 그를 구비한 슬러리 공급 시스템 |
GB201908449D0 (en) | 2019-06-12 | 2019-07-24 | Johnson Matthey Davy Technologies Ltd | Process for synthesising methanol |
GB201908450D0 (en) | 2019-06-12 | 2019-07-24 | Johnson Matthey Davy Technologies Ltd | Process for synthesising methanol |
FR3103714B1 (fr) | 2019-11-28 | 2021-12-03 | Commissariat Energie Atomique | Reacteur tubulaire a lit fixe |
EP4277736A1 (en) * | 2021-01-15 | 2023-11-22 | Cri Hf | Methanol synthesis reactor |
EP4321245A4 (en) * | 2021-04-09 | 2025-04-23 | China Petroleum & Chemical Corporation | Heat removal pipe group, method for controlling reaction temperature, and method for fabricating unsaturated nitriles |
WO2022238671A1 (en) | 2021-05-11 | 2022-11-17 | Johnson Matthey Davy Technologies Limited | Process for synthesising methanol |
EP4337629A1 (en) | 2021-05-11 | 2024-03-20 | Johnson Matthey Davy Technologies Limited | Process for synthesising methanol |
GB202109905D0 (en) | 2021-07-09 | 2021-08-25 | Johnson Matthey Plc | Process for synthesising methanol |
FR3140155B1 (fr) | 2022-09-26 | 2024-10-25 | Commissariat Energie Atomique | Réacteur-échangeur à lit fixe muni d’au moins une grille à barreaux creux de circulation d’un fluide caloporteur. |
GB202217131D0 (en) | 2022-11-16 | 2022-12-28 | Johnson Matthey Davy Technologies Ltd | Methanol process |
GB202400240D0 (en) | 2024-01-08 | 2024-02-21 | Johnson Matthey Davy Technologies Ltd | Process for synthesising methanol |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2450804A (en) * | 1943-12-09 | 1948-10-05 | Phillips Petroleum Co | Catalyst chamber construction |
US2664346A (en) * | 1950-06-22 | 1953-12-29 | Hydrocarbon Research Inc | Fluid reactor |
US2744813A (en) * | 1951-10-06 | 1956-05-08 | Ruhrchemie Ag | Catalytic furnace |
US2997374A (en) * | 1958-03-13 | 1961-08-22 | California Research Corp | Radial flow reactor |
US3466152A (en) * | 1965-07-28 | 1969-09-09 | Ube Kogyo Kk | Synthetizing reactor equipped with temperature control device for catalyst layer |
US3907665A (en) * | 1972-10-26 | 1975-09-23 | Universal Oil Prod Co | Dehydrogenation process |
US3944394A (en) * | 1974-10-31 | 1976-03-16 | Phillips Petroleum Company | Apparatus suitable for carrying out catalytic process |
-
1979
- 1979-04-03 JP JP54039306A patent/JPS5839572B2/ja not_active Expired
-
1980
- 1980-03-18 AU AU56562/80A patent/AU526051B2/en not_active Ceased
- 1980-03-20 IN IN327/CAL/80A patent/IN152670B/en unknown
- 1980-03-31 GB GB8010761A patent/GB2046618B/en not_active Expired
- 1980-03-31 DE DE19803012476 patent/DE3012476A1/de not_active Withdrawn
- 1980-04-01 CS CS802260A patent/CS221542B2/cs unknown
- 1980-04-02 NL NL8001940A patent/NL8001940A/nl not_active Application Discontinuation
- 1980-04-02 DD DD80220171A patent/DD150006A5/de unknown
- 1980-04-02 BE BE0/200081A patent/BE882591A/fr not_active IP Right Cessation
- 1980-04-02 AR AR280549A patent/AR223213A1/es active
- 1980-04-02 MX MX181845A patent/MX155157A/es unknown
- 1980-04-02 RO RO100696A patent/RO81469B/ro unknown
- 1980-04-02 CA CA000349102A patent/CA1160817A/en not_active Expired
- 1980-04-02 BR BR8002067A patent/BR8002067A/pt not_active IP Right Cessation
- 1980-04-03 FR FR8007616A patent/FR2452964B1/fr not_active Expired
- 1980-04-03 IT IT8021172A patent/IT1209201B/it active
- 1980-04-03 PL PL1980223226A patent/PL124655B1/pl unknown
- 1980-12-22 US US06/219,359 patent/US4321234A/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
PL223226A1 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html) | 1981-02-13 |
AR223213A1 (es) | 1981-07-31 |
CS221542B2 (en) | 1983-04-29 |
US4321234A (en) | 1982-03-23 |
GB2046618B (en) | 1983-08-24 |
IT8021172A0 (it) | 1980-04-03 |
IN152670B (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html) | 1984-03-10 |
BR8002067A (pt) | 1980-11-25 |
DE3012476A1 (de) | 1980-10-16 |
AU526051B2 (en) | 1982-12-16 |
NL8001940A (nl) | 1980-10-07 |
IT1209201B (it) | 1989-07-16 |
CA1160817A (en) | 1984-01-24 |
PL124655B1 (en) | 1983-02-28 |
JPS5839572B2 (ja) | 1983-08-31 |
GB2046618A (en) | 1980-11-19 |
AU5656280A (en) | 1980-10-09 |
MX155157A (es) | 1988-02-01 |
FR2452964A1 (fr) | 1980-10-31 |
RO81469B (ro) | 1983-04-30 |
RO81469A (ro) | 1983-04-29 |
BE882591A (fr) | 1980-07-31 |
FR2452964B1 (fr) | 1986-12-19 |
JPS55149640A (en) | 1980-11-21 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DD150006A5 (de) | Chemisches verfahren und reaktionsgefaess fuer die durchfuehrung desselben | |
DE3414717C2 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html) | ||
DE3334775C2 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html) | ||
DE69420604T2 (de) | Vorrichtung zur Herstellung von Wasserstoff | |
DE60129686T2 (de) | Reaktor für exothermische oder endothermische heterogene reaktionen | |
EP0396650B2 (de) | Vorrichtung zur durchführung katalysierter reaktionen | |
DE69000483T2 (de) | Vorrichtung und verfahren fuer exothermische reaktionen. | |
EP3497058B1 (de) | Synthesevorrichtung und verfahren zur herstellung eines produkts | |
DE2815856A1 (de) | Reaktor | |
EP1232004A1 (de) | Verfahren zur katalytischen gasphasenoxidation zu (meth)acrolein und/oder (meth)acrylsäure | |
EP1185494B1 (de) | Verfahren zur katalytischen gasphasenoxidation zu maleinsäureanhydrid | |
DD219758A5 (de) | Verfahren zur herstellung eines methan enthaltenden gases | |
DE69732781T2 (de) | Verfahren zur in-situ Modernisierung eines heterogenen exothermen Synthesereaktors | |
DD283678A5 (de) | Waermeaustauschvorrichtung sowie ein waermeaustauschverfahren | |
DE2742204A1 (de) | Reaktor fuer katalytische exotherme reaktionen | |
DE3832257A1 (de) | Katalysator-festbettreaktor | |
DE2420949C3 (de) | Verfahren und Reaktor zur Herstellung von Äthylenoxid durch katalytische Oxidation von Äthylen | |
DE3442053C2 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html) | ||
DE2631884A1 (de) | Dampf-kohlenwasserstoff-reformiereinrichtung | |
WO2006069694A1 (de) | Verfahren zur herstellung von phthalsäureanhydrid | |
DE2502274A1 (de) | Verfahren zur waermeregelung von bei hoher temperatur arbeitenden katalytischen wirbelbettreaktoren | |
DE60107951T2 (de) | Gerät und verfahren zur herstellung von formaldehyd | |
DD150006C4 (de) | Chemisches verfahren und reaktionsgefaess fuer die durchfuehrung desselben | |
WO1998050375A1 (de) | Verfahren und reaktor zur herstellung von ethylenoxid | |
DE853441C (de) | Reaktionskammer zur Regelung der Temperatur von exothermen und endothermen Reaktionen |