WO1985003291A1 - Process for obtention of phthalimide - Google Patents
Process for obtention of phthalimide Download PDFInfo
- Publication number
- WO1985003291A1 WO1985003291A1 PCT/SU1984/000002 SU8400002W WO8503291A1 WO 1985003291 A1 WO1985003291 A1 WO 1985003291A1 SU 8400002 W SU8400002 W SU 8400002W WO 8503291 A1 WO8503291 A1 WO 8503291A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- πρi
- mass
- carbamide
- pressure
- mixture
- Prior art date
Links
- XKJCHHZQLQNZHY-UHFFFAOYSA-N phthalimide Chemical compound C1=CC=C2C(=O)NC(=O)C2=C1 XKJCHHZQLQNZHY-UHFFFAOYSA-N 0.000 title abstract description 4
- 238000000034 method Methods 0.000 title description 13
- 235000009421 Myristica fragrans Nutrition 0.000 claims 2
- 239000001115 mace Substances 0.000 claims 2
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 abstract description 34
- 239000004202 carbamide Substances 0.000 abstract description 17
- 235000013877 carbamide Nutrition 0.000 abstract description 17
- 238000003756 stirring Methods 0.000 abstract description 7
- LGRFSURHDFAFJT-UHFFFAOYSA-N Phthalic anhydride Natural products C1=CC=C2C(=O)OC(=O)C2=C1 LGRFSURHDFAFJT-UHFFFAOYSA-N 0.000 abstract description 4
- JHIWVOJDXOSYLW-UHFFFAOYSA-N butyl 2,2-difluorocyclopropane-1-carboxylate Chemical compound CCCCOC(=O)C1CC1(F)F JHIWVOJDXOSYLW-UHFFFAOYSA-N 0.000 abstract description 4
- 239000003153 chemical reaction reagent Substances 0.000 abstract description 3
- 230000003993 interaction Effects 0.000 abstract description 3
- 239000000203 mixture Substances 0.000 description 17
- 239000000047 product Substances 0.000 description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 7
- 239000002253 acid Substances 0.000 description 7
- 239000007789 gas Substances 0.000 description 7
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- 150000008064 anhydrides Chemical class 0.000 description 6
- 238000002844 melting Methods 0.000 description 6
- 230000008018 melting Effects 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 4
- 229910021529 ammonia Inorganic materials 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000013067 intermediate product Substances 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000011541 reaction mixture Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- KPYCVQASEGGKEG-UHFFFAOYSA-N 3-hydroxyoxolane-2,5-dione Chemical compound OC1CC(=O)OC1=O KPYCVQASEGGKEG-UHFFFAOYSA-N 0.000 description 1
- 150000008065 acid anhydrides Chemical class 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 230000037406 food intake Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000010309 melting process Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000007420 reactivation Effects 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000000859 sublimation Methods 0.000 description 1
- 230000008022 sublimation Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D209/00—Heterocyclic compounds containing five-membered rings, condensed with other rings, with one nitrogen atom as the only ring hetero atom
- C07D209/02—Heterocyclic compounds containing five-membered rings, condensed with other rings, with one nitrogen atom as the only ring hetero atom condensed with one carbocyclic ring
- C07D209/44—Iso-indoles; Hydrogenated iso-indoles
- C07D209/48—Iso-indoles; Hydrogenated iso-indoles with oxygen atoms in positions 1 and 3, e.g. phthalimide
Definitions
- the product is isolated from the suspension by dosing, the plant is washed away from the water for drying and drying.
- the output of phthalimide is 90-96 $ from the theory, the melting point is 232-235 ° C (patent USL L 3819648, CL 260-326, published 1975).
- the capacitive appliance with a stirrer, a disassembler, a socket and a built-in serpentine loads the carbamide, disables its agitator, loads an unloading, and unloads
- the high ratio between phthalic anhydride and carbamide is 1: 0.8; the coefficient of loading the reaction is 0.15.
- the appliance and the coil of the appliance are fed with the process coupler with the transmitter - 2 - ⁇ ⁇ 80 ° ⁇ . Upon reaching a reactionary mixture of ⁇ 30- ⁇ 35 ° C, carbamide is decomposed, and reactivation of the reaction begins.
- the resulting macebide is water-borne, it is cooked for 2–30 minutes and turns on the stirrer. If the m ⁇ -shuffle is not pumped, the mass of the manual b ⁇ for the hatch is six. The mixed mass is stirred for 30-60 minutes, the resulting suspension of the centrifuge is removed, the plant is washed with water and discharged.
- the temperature of the product is $ 91-92, the melting point is 232-237 ° ⁇ , the moisture content is $ 4-6.
- Raw materials of raw materials make up the total anhydride II 00 kg / t, and for the carbamide - 375 kg / t.
- Waste water for the supply of suction and washing the precipitate is 9000 kg / t, a large amount of water - 9250 kg / t, because there is a lot of waste gas - 150
- the object of the present invention is the compilation of the phthalimide device, which is respected by the user.
- ⁇ azvannaya task ⁇ sha ⁇ sya ⁇ m, ch ⁇ ⁇ i ⁇ luchenii ⁇ adimida ⁇ u ⁇ em vzaim ⁇ d ⁇ ys ⁇ viya ⁇ al ⁇ v ⁇ g ⁇ angid ⁇ ida with ⁇ a ⁇ bamid ⁇ m ⁇ i nag ⁇ evanii, s ⁇ glasn ⁇ nas ⁇ yasch ⁇ mu iz ⁇ b ⁇ - ⁇ eniyu, ⁇ alevy angid ⁇ id and ⁇ a ⁇ bamid is ⁇ lzuyu ⁇ in ⁇ li- ches ⁇ ve, ⁇ i ⁇ m i ⁇ m ⁇ ln ⁇ e s ⁇ n ⁇ sheni ⁇ s ⁇ e ⁇ avlya ⁇ 1: 0.5-0.7, s ⁇ ve ⁇ s ⁇ venn ⁇ , ⁇ ts ⁇ ss vedu ⁇ ⁇ i ⁇ s ⁇ yan- n ⁇ m ⁇ e ⁇ em ⁇ shivanii ⁇ a
- the download factor of the mixer is equal to 0.6-0.7.
- ⁇ the temperature is ⁇ 5- ⁇ 25- ⁇ 30 ° C, which is prevented by the operation of the device and the device is in contact with the device, and the device is inaccessible to the user, and the device is inaccessible to the user.
- P ⁇ i d ⁇ s ⁇ izhenii ⁇ m ⁇ e ⁇ a ⁇ u ⁇ y ⁇ 25- ⁇ 30 ° C nachinae ⁇ sya ⁇ ts ⁇ ss ⁇ b ⁇ az ⁇ vaniya ⁇ alimida, s ⁇ v ⁇ zhdaschiysya vyd ⁇ deniem ⁇ e ⁇ - la and in ⁇ ensivnym gas evolution ugle ⁇ isl ⁇ g ⁇ , ⁇ a ⁇ v ⁇ ea ⁇ tsi ⁇ nn ⁇ y v ⁇ dy and u 'zby ⁇ chn ⁇ g ⁇ ammia ⁇ a.
- the volume of the puffed mass is, therefore, instantly increased up to ⁇ 50- ⁇ 60 ° ⁇ , and then it decreases by 5- ⁇ raum ⁇ .
- the inactive mass in this unit provides a dry, small-sized phthadimide with the exclusion of separate large-sized external salts. You save up to ⁇ 50- ⁇ 70 ° C, keep it at the indicated temperature a minute before you take out the ammunition, it takes out the load. - 5 -
- the mixer is equipped with electronic accessories, a unit for cooling and cooling, and a cavity that has a connection for loading 20 generations, a partition is available. After the charge is turned on, the mixture is pressurized, the mixer is set to a pressure of 0.090-0.098 ⁇ Pa and the mixture is heated, the mixture is heated to a temperature of 0 ° C. The resulting heaters give a heat of 25 ° C to 55 ° C and maintain a specified heat of 60 minutes. At the end of the batch, the obtained product and stirring waits for the room temperature.
- Example 3 in a mixture, heated to a mixture of 6 ⁇ -90 ° ⁇ , load 444.36 g (3 mol) of anhydrous acid and 126.1 g of carbamide (2, 1 med); ), pressurizes the mixer, creates a residual pressure of 0 0, 090-0, 098 réelle Pa and stirs it. At 95–5 ° C, the mixture is melted, the resulting melt is heated to 70 ° 0 and is kept at this temperature for 10–15 minutes. At the end of the batch, the waste mass is cooled and mixed until the room temperature is very high.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Indole Compounds (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
Priority Applications (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB08522752A GB2162848B (en) | 1984-01-23 | 1984-01-23 | Process for obtention of phthalimide |
HU843232A HU194826B (en) | 1984-01-23 | 1984-01-23 | Process for producing phtalimide |
JP59502893A JPS61501028A (ja) | 1984-01-23 | 1984-01-23 | フタルイミドの調製方法 |
DE19843490634 DE3490634T1 (de) | 1984-01-23 | 1984-01-23 | Verfahren zur Herstellung von Phthalimid |
DE19843490634 DE3490634C2 (de) | 1984-01-23 | 1984-01-23 | Verfahren zur Herstellung von Phthalimid |
PCT/SU1984/000002 WO1985003291A1 (en) | 1984-01-23 | 1984-01-23 | Process for obtention of phthalimide |
CH415785A CH665416A5 (de) | 1984-01-23 | 1984-01-23 | Verfahren zur herstellung von phthalimid. |
IN297/CAL/84A IN161812B (enrdf_load_stackoverflow) | 1981-06-29 | 1984-05-03 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/SU1984/000002 WO1985003291A1 (en) | 1984-01-23 | 1984-01-23 | Process for obtention of phthalimide |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1985003291A1 true WO1985003291A1 (en) | 1985-08-01 |
Family
ID=21616832
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/SU1984/000002 WO1985003291A1 (en) | 1981-06-29 | 1984-01-23 | Process for obtention of phthalimide |
Country Status (6)
Country | Link |
---|---|
JP (1) | JPS61501028A (enrdf_load_stackoverflow) |
CH (1) | CH665416A5 (enrdf_load_stackoverflow) |
DE (2) | DE3490634C2 (enrdf_load_stackoverflow) |
GB (1) | GB2162848B (enrdf_load_stackoverflow) |
HU (1) | HU194826B (enrdf_load_stackoverflow) |
WO (1) | WO1985003291A1 (enrdf_load_stackoverflow) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2185376C1 (ru) * | 2001-01-03 | 2002-07-20 | Волгоградское открытое акционерное общество "Химпром" | Способ получения фталимида |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4001273A (en) * | 1973-07-10 | 1977-01-04 | Basf Aktiengesellschaft | Continuous manufacture of phthalimide |
US4020089A (en) * | 1975-07-01 | 1977-04-26 | General Electric Company | Method for making n-alkylphthalimides |
-
1984
- 1984-01-23 CH CH415785A patent/CH665416A5/de not_active IP Right Cessation
- 1984-01-23 JP JP59502893A patent/JPS61501028A/ja active Granted
- 1984-01-23 WO PCT/SU1984/000002 patent/WO1985003291A1/ru active Application Filing
- 1984-01-23 DE DE19843490634 patent/DE3490634C2/de not_active Expired
- 1984-01-23 DE DE19843490634 patent/DE3490634T1/de active Pending
- 1984-01-23 HU HU843232A patent/HU194826B/hu not_active IP Right Cessation
- 1984-01-23 GB GB08522752A patent/GB2162848B/en not_active Expired
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4001273A (en) * | 1973-07-10 | 1977-01-04 | Basf Aktiengesellschaft | Continuous manufacture of phthalimide |
US4020089A (en) * | 1975-07-01 | 1977-04-26 | General Electric Company | Method for making n-alkylphthalimides |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2185376C1 (ru) * | 2001-01-03 | 2002-07-20 | Волгоградское открытое акционерное общество "Химпром" | Способ получения фталимида |
Also Published As
Publication number | Publication date |
---|---|
GB2162848A (en) | 1986-02-12 |
HUT38311A (en) | 1986-05-28 |
DE3490634C2 (de) | 1989-03-09 |
GB8522752D0 (en) | 1985-10-16 |
JPS61501028A (ja) | 1986-05-22 |
DE3490634T1 (de) | 1986-01-09 |
HU194826B (en) | 1988-03-28 |
CH665416A5 (de) | 1988-05-13 |
GB2162848B (en) | 1987-06-10 |
JPH0255421B2 (enrdf_load_stackoverflow) | 1990-11-27 |
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