WO1985003291A1 - Procede d'obtention de phtalimides - Google Patents
Procede d'obtention de phtalimides 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
- 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.)
- Ceased
Links
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 |
|---|---|---|---|
| DE19843490634 DE3490634C2 (de) | 1984-01-23 | 1984-01-23 | Verfahren zur Herstellung von Phthalimid |
| PCT/SU1984/000002 WO1985003291A1 (fr) | 1984-01-23 | 1984-01-23 | Procede d'obtention de phtalimides |
| 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 |
| HU843232A HU194826B (en) | 1984-01-23 | 1984-01-23 | Process for producing phtalimide |
| GB08522752A GB2162848B (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 (enExample) | 1981-06-29 | 1984-05-03 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/SU1984/000002 WO1985003291A1 (fr) | 1984-01-23 | 1984-01-23 | Procede d'obtention de phtalimides |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1985003291A1 true WO1985003291A1 (fr) | 1985-08-01 |
Family
ID=21616832
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/SU1984/000002 Ceased WO1985003291A1 (fr) | 1981-06-29 | 1984-01-23 | Procede d'obtention de phtalimides |
Country Status (6)
| Country | Link |
|---|---|
| JP (1) | JPS61501028A (enExample) |
| CH (1) | CH665416A5 (enExample) |
| DE (2) | DE3490634T1 (enExample) |
| GB (1) | GB2162848B (enExample) |
| HU (1) | HU194826B (enExample) |
| WO (1) | WO1985003291A1 (enExample) |
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 DE DE19843490634 patent/DE3490634T1/de active Pending
- 1984-01-23 GB GB08522752A patent/GB2162848B/en not_active Expired
- 1984-01-23 JP JP59502893A patent/JPS61501028A/ja active Granted
- 1984-01-23 DE DE19843490634 patent/DE3490634C2/de not_active Expired
- 1984-01-23 HU HU843232A patent/HU194826B/hu not_active IP Right Cessation
- 1984-01-23 CH CH415785A patent/CH665416A5/de not_active IP Right Cessation
- 1984-01-23 WO PCT/SU1984/000002 patent/WO1985003291A1/ru not_active Ceased
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 |
|---|---|
| HU194826B (en) | 1988-03-28 |
| HUT38311A (en) | 1986-05-28 |
| DE3490634T1 (de) | 1986-01-09 |
| GB8522752D0 (en) | 1985-10-16 |
| JPS61501028A (ja) | 1986-05-22 |
| GB2162848B (en) | 1987-06-10 |
| JPH0255421B2 (enExample) | 1990-11-27 |
| CH665416A5 (de) | 1988-05-13 |
| DE3490634C2 (de) | 1989-03-09 |
| GB2162848A (en) | 1986-02-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4839461A (en) | Polyaspartic acid from maleic acid and ammonia | |
| EP0330220A2 (en) | Process for the preparation and recovery of oxydiphthalic anhydrides | |
| WO1985003291A1 (fr) | Procede d'obtention de phtalimides | |
| US2864871A (en) | Method of producing dinitro-tetra alkyl benzenes | |
| SU1509352A1 (ru) | Способ получени 4,4 @ -(арилендиокси)-дифталонитрилов | |
| US4690785A (en) | Low water neutralization to produce a highly active alkaryl sulfonate | |
| US2389950A (en) | Production of di-carboxylic acids | |
| JPH01311123A (ja) | ポリイミド前駆物質組成物 | |
| CN102909074B (zh) | 固载型无毒催化剂及其合成n-苯基马来酰亚胺和n-苯基取代马来酰亚胺中的方法 | |
| CN106277477A (zh) | 一种2,4‑二氨基苯磺酸及其盐生产过程中含酸废水的处理方法 | |
| JP2853521B2 (ja) | ジニトロ−ポリアルキルベンゼン類の製造方法 | |
| SU1077233A1 (ru) | Способ получени фталимида | |
| US3366692A (en) | Process for preparing 4, 4'-dihydroxydiphenyl sulfone | |
| US5994561A (en) | Process for the preparation of aromatic maleimides | |
| CN112661633A (zh) | 一种连续制备抗氧剂1010的方法 | |
| US2502748A (en) | Production of magnesium phthalocyanine | |
| US2697102A (en) | Production of the exocis isomer of 3, 6-endoxo-1, 2, 3, 6-tetrahydrophthalic anhydride | |
| JPS5929676A (ja) | アムメリド・メラミン付加物の製造方法 | |
| RU2291856C1 (ru) | Способ получения формиата железа (ii) | |
| RU2359956C1 (ru) | Способ получения оксалата марганца (ii) | |
| FR2583748A1 (fr) | Procede de preparation de sels du sel disodique de l'acide ethylenediamine-tetra-acetique, et de leurs hydrates | |
| JPS60112759A (ja) | Ν−フエニルマレイミド類の製造法 | |
| SU1505904A1 (ru) | Способ приготовлени жидкой магнийфосфатной св зки | |
| JPS6152831B2 (enExample) | ||
| JPS6092245A (ja) | ジアルキルサクシニルサクシネ−トの製造法 |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AK | Designated states |
Designated state(s): CH DE GB HU JP US |
|
| RET | De translation (de og part 6b) |
Ref document number: 3490634 Country of ref document: DE Date of ref document: 19860109 |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 3490634 Country of ref document: DE |