BE658512A - - Google Patents
Info
- Publication number
- BE658512A BE658512A BE658512DA BE658512A BE 658512 A BE658512 A BE 658512A BE 658512D A BE658512D A BE 658512DA BE 658512 A BE658512 A BE 658512A
- Authority
- BE
- Belgium
- Prior art keywords
- heat
- chlorinated
- heat exchange
- gas
- tower
- Prior art date
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 34
- 239000007789 gas Substances 0.000 claims description 30
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N diphenyl Chemical group C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 claims description 24
- 239000000463 material Substances 0.000 claims description 22
- QDHHCQZDFGDHMP-UHFFFAOYSA-N monochloramine Chemical compound ClN QDHHCQZDFGDHMP-UHFFFAOYSA-N 0.000 claims description 14
- 239000000567 combustion gas Substances 0.000 claims description 10
- 229920002178 Polyphenyl ether Polymers 0.000 claims description 9
- 235000010290 biphenyl Nutrition 0.000 claims description 7
- 239000000460 chlorine Substances 0.000 claims description 6
- 229910052801 chlorine Inorganic materials 0.000 claims description 6
- ZAMOUSCENKQFHK-UHFFFAOYSA-N chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 claims description 6
- RGCAQUUSBHVLJD-UHFFFAOYSA-N 1-phenoxy-4-(4-phenoxyphenyl)benzene Chemical group C=1C=C(C=2C=CC(OC=3C=CC=CC=3)=CC=2)C=CC=1OC1=CC=CC=C1 RGCAQUUSBHVLJD-UHFFFAOYSA-N 0.000 claims description 5
- 238000000034 method Methods 0.000 claims description 4
- 239000003546 flue gas Substances 0.000 claims description 3
- 239000004305 biphenyl Substances 0.000 claims description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims 1
- 230000000630 rising Effects 0.000 claims 1
- 238000011084 recovery Methods 0.000 description 23
- 239000012530 fluid Substances 0.000 description 19
- 239000007788 liquid Substances 0.000 description 10
- 150000001875 compounds Chemical class 0.000 description 8
- 239000000203 mixture Substances 0.000 description 7
- -1 m-phenoxyphenyl Chemical group 0.000 description 6
- 150000002894 organic compounds Chemical class 0.000 description 6
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 5
- 150000004074 biphenyls Chemical class 0.000 description 5
- 230000000875 corresponding Effects 0.000 description 5
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 5
- 239000000446 fuel Substances 0.000 description 5
- 238000009434 installation Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- FJKZXJNLYCXUEW-UHFFFAOYSA-N 1,1'-biphenyl;ethoxyethane Chemical compound CCOCC.C1=CC=CC=C1C1=CC=CC=C1 FJKZXJNLYCXUEW-UHFFFAOYSA-N 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- RELMFMZEBKVZJC-UHFFFAOYSA-N 1,2,3-trichlorobenzene Chemical compound ClC1=CC=CC(Cl)=C1Cl RELMFMZEBKVZJC-UHFFFAOYSA-N 0.000 description 2
- AKEJUJNQAAGONA-UHFFFAOYSA-N Sulfur trioxide Chemical compound O=S(=O)=O AKEJUJNQAAGONA-UHFFFAOYSA-N 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000006011 modification reaction Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- PBKONEOXTCPAFI-UHFFFAOYSA-N 1,2,4-Trichlorobenzene Chemical compound ClC1=CC=C(Cl)C(Cl)=C1 PBKONEOXTCPAFI-UHFFFAOYSA-N 0.000 description 1
- FIPTYOFKSOWKTF-UHFFFAOYSA-N 1,2-diphenoxybenzene Chemical compound C=1C=CC=C(OC=2C=CC=CC=2)C=1OC1=CC=CC=C1 FIPTYOFKSOWKTF-UHFFFAOYSA-N 0.000 description 1
- YJTKZCDBKVTVBY-UHFFFAOYSA-N 1,3-Diphenylbenzene Chemical group C1=CC=CC=C1C1=CC=CC(C=2C=CC=CC=2)=C1 YJTKZCDBKVTVBY-UHFFFAOYSA-N 0.000 description 1
- JTNRGGLCSLZOOQ-UHFFFAOYSA-N 1,3-diphenoxybenzene Chemical compound C=1C=CC(OC=2C=CC=CC=2)=CC=1OC1=CC=CC=C1 JTNRGGLCSLZOOQ-UHFFFAOYSA-N 0.000 description 1
- UVGPELGZPWDPFP-UHFFFAOYSA-N 1,4-diphenoxybenzene Chemical compound C=1C=C(OC=2C=CC=CC=2)C=CC=1OC1=CC=CC=C1 UVGPELGZPWDPFP-UHFFFAOYSA-N 0.000 description 1
- QKHCUKLDPPXGFA-UHFFFAOYSA-N 1-phenoxy-2-(2-phenoxyphenoxy)benzene Chemical compound C=1C=CC=C(OC=2C(=CC=CC=2)OC=2C=CC=CC=2)C=1OC1=CC=CC=C1 QKHCUKLDPPXGFA-UHFFFAOYSA-N 0.000 description 1
- UHJWZORSTYATLW-UHFFFAOYSA-N 1-phenoxy-2-phenylbenzene Chemical group C=1C=CC=C(C=2C=CC=CC=2)C=1OC1=CC=CC=C1 UHJWZORSTYATLW-UHFFFAOYSA-N 0.000 description 1
- MVCITNPWSJQCBC-UHFFFAOYSA-N 1-phenoxy-3-(3-phenoxyphenoxy)benzene Chemical compound C=1C=CC(OC=2C=C(OC=3C=CC=CC=3)C=CC=2)=CC=1OC1=CC=CC=C1 MVCITNPWSJQCBC-UHFFFAOYSA-N 0.000 description 1
- GQGTXJRZSBTHOB-UHFFFAOYSA-N 1-phenoxy-4-(4-phenoxyphenoxy)benzene Chemical compound C=1C=C(OC=2C=CC(OC=3C=CC=CC=3)=CC=2)C=CC=1OC1=CC=CC=C1 GQGTXJRZSBTHOB-UHFFFAOYSA-N 0.000 description 1
- USIUVYZYUHIAEV-UHFFFAOYSA-N Diphenyl ether Chemical compound C=1C=CC=CC=1OC1=CC=CC=C1 USIUVYZYUHIAEV-UHFFFAOYSA-N 0.000 description 1
- 241000238631 Hexapoda Species 0.000 description 1
- WXJFJZQIDLQFIJ-UHFFFAOYSA-N O(C1=CC=CC=C1)C1=C(C(=C(C=C1)OC1=C(C(=C(C=C1)OC1=CC=CC=C1)C1=CC=CC=C1)OC1=CC=CC=C1)OC1=CC=CC=C1)C1=CC=CC=C1 Chemical compound O(C1=CC=CC=C1)C1=C(C(=C(C=C1)OC1=C(C(=C(C=C1)OC1=CC=CC=C1)C1=CC=CC=C1)OC1=CC=CC=C1)OC1=CC=CC=C1)C1=CC=CC=C1 WXJFJZQIDLQFIJ-UHFFFAOYSA-N 0.000 description 1
- XZZNDPSIHUTMOC-UHFFFAOYSA-N Triphenyl phosphate Chemical compound C=1C=CC=CC=1OP(OC=1C=CC=CC=1)(=O)OC1=CC=CC=C1 XZZNDPSIHUTMOC-UHFFFAOYSA-N 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 125000006267 biphenyl group Chemical group 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000014509 gene expression Effects 0.000 description 1
- 238000005304 joining Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000012074 organic phase Substances 0.000 description 1
- 230000001590 oxidative Effects 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 125000004430 oxygen atoms Chemical group O* 0.000 description 1
- 230000000149 penetrating Effects 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000011369 resultant mixture Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000008207 working material Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
- F22B1/18—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
- F22B1/1853—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines coming in direct contact with water in bulk or in sprays
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Treating Waste Gases (AREA)
Publications (1)
| Publication Number | Publication Date |
|---|---|
| BE658512A true BE658512A (zh) |
Family
ID=206894
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| BE658512D BE658512A (zh) |
Country Status (1)
| Country | Link |
|---|---|
| BE (1) | BE658512A (zh) |
-
0
- BE BE658512D patent/BE658512A/fr unknown
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| RU2549876C2 (ru) | Система высушивания биомассы (варианты) | |
| EP0691155B1 (fr) | Procédé de désacidification d'un gaz pour production de gaz acides concentrés | |
| US20170283714A1 (en) | Waste to Fuel System | |
| EP0368964B1 (fr) | Procede d'extraction de l'eau melangee a un fluide liquide | |
| FR2740131A1 (fr) | Procede de production d'acetylene et de gaz de synthese | |
| US20150184098A1 (en) | Biomass Bio Oil Upgrade Method | |
| EP3476468B1 (fr) | Dispositif pour la gazeification en milieu supercritique d'un effluent aqueux | |
| US20150183961A1 (en) | Biomass Processing | |
| US20150184025A1 (en) | Biomass Bio Oil Upgrade Method | |
| BE658512A (zh) | ||
| CN103555351B (zh) | 一种林农废弃物自热式热解装置 | |
| CN102203044A (zh) | 采用增强的能量回收法制备二羧酸 | |
| CN212881109U (zh) | 一种精馏预塔放空气处理装置 | |
| FR2844804A1 (fr) | Procede et installation de valorisation de sous-produits a base de matieres organiques | |
| FR2474646A2 (fr) | Procede d'obtention simultanee et rentable de sources d'energie, d'eau douce et de sous-produits a partir de substances aqueuses et d'une source d'energie | |
| US3249152A (en) | Heat recovery process | |
| CN102203045A (zh) | 采用自供燃料氧化性分解制备二羧酸 | |
| US3258063A (en) | Heat recovery process | |
| US3249151A (en) | Heat recovery process | |
| Spitsyn et al. | Ultrapyrolysis of wood biomass for production of ecologically clean boiler fuels and motor fuels | |
| FR3126126A1 (fr) | Procédé et dispositif de production de produits énergétiques par craquage catalytique d’un matériau solide hydrocarboné sans formation de coke | |
| BE385802A (zh) | ||
| CN102203046A (zh) | 采用直接燃烧废气加热法的二羧酸制备 | |
| CN102203043A (zh) | 产生最少量废水的二羧酸制备方法 | |
| EP3660131A1 (fr) | Procédé d'obtention d'un biobrut par pyrolyse et hydroliquefaction d'une biomasse |