FIELD: chemical industry. SUBSTANCE: evaporator uses descending current heating chamber 1, ascending current heating chamber 2, boiling pipe 3, separator 4, circulating pump 5, intermediate vessel crystallizer 6. Vessel 6 accommodates the end of the transfer pipe, whose lower end is provided with a swirler of evaporated solution made in the form of a cylinder with a spherical bottom, whose camber faces upwards and whose side walls have ports. These ports are made as nicks with C-shaped bends oriented inside the cylinder in the direction of flow. Throttling orifice 19 is installed at the outlet of chamber 2. Intermediate vessel 6 has a cooling jacket. EFFECT: decreased overall dimensions and specific consumption of materials, more complete removal of salt crystals from evaporated solution. 3 cl, 4 dwg
Title | Year | Author | Number |
---|---|---|---|
EVAPORATOR FOR SALT-BEARING SOLUTIONS | 1991 |
|
RU2050164C1 |
EVAPORATOR | 2004 |
|
RU2257245C1 |
FORCED-CIRCULATION EVAPORATOR FOR ALUMINATE SOLUTIONS | 1993 |
|
RU2082476C1 |
EVAPORATION APPARATUS FOR SALT-CONTAINING SOLUTIONS | 0 |
|
SU1468555A1 |
EVAPORATION APPARATUS FOR SALT-CONTAINING SOLUTIONS | 0 |
|
SU1468554A2 |
CRYSTALLIZING EVAPORATOR | 2005 |
|
RU2301698C1 |
PLANT FOR LIQUID PURIFICATION | 1993 |
|
RU2039709C1 |
SOLUTION CRYSTALLISATION APPARATUS | 2006 |
|
RU2341316C2 |
EVAPORATION APPARATUS FOR SALT CONTAINING SOLUTIONS | 0 |
|
SU1005802A1 |
EVAPORATION APPARATUS FOR SALT-CONTAINING SOLUTIONS | 0 |
|
SU1230612A1 |
Authors
Dates
1995-12-10—Published
1992-05-21—Filed