ES393643A1 - Multi-level spray drying method - Google Patents
Multi-level spray drying methodInfo
- Publication number
- ES393643A1 ES393643A1 ES393643A ES393643A ES393643A1 ES 393643 A1 ES393643 A1 ES 393643A1 ES 393643 A ES393643 A ES 393643A ES 393643 A ES393643 A ES 393643A ES 393643 A1 ES393643 A1 ES 393643A1
- Authority
- ES
- Spain
- Prior art keywords
- drying zone
- drying
- cylindrical
- practically
- slurry
- 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.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D11/00—Special methods for preparing compositions containing mixtures of detergents ; Methods for using cleaning compositions
- C11D11/02—Preparation in the form of powder by spray drying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/16—Evaporating by spraying
- B01D1/18—Evaporating by spraying to obtain dry solids
Abstract
Continuous process for the spray drying of large volumes of a synthetic detergent slurry, in a spray drying tower and for the production of a granular composition of synthetic detergents that has a controlled density and a reduced and uniform particle size, with minimal production of dust particles and other gaseous effluents; characterized in that it comprises the following steps: (1) preparing an aqueous slurry of synthetic detergent having approximately 10 to 50% by weight of water and a solids content of 50 to 90%, said slurry being composed of at least an organic synthetic detergent and at least one detergent additive selected from organic or inorganic additives and mixtures thereof; (2) establishing inside the chamber of the spray tower (a) a drying zone of cylindrical configuration passing through the axis of the chamber hot drying air up through said chamber in a cyclonic movement and (b) a low pressure zone comprising a concentric vortex tube that is formed along the axis of the chamber; (3) continuously spraying 30 to 80% of said synthetic detergent slurry in countercurrent directly in the drying zone of cylindrical configuration; at the point below an isotherm of 87.8ºC and above an isotherm of the boiling point, said spraying being achieved with atomizing nozzles evenly spaced practically in a horizontal plane through the cylindrical drying zone, thereby providing the that practically each of the sprays disintegrates into particles within said cylindrical drying zone; (4) continuously spray counter-current the rest of said synthetic detergent slurry directly into the cylindrical configuration drying zone at a point above the 87.8ºC isotherm by means of at least one level of atomizing nozzles evenly spaced, practically in a horizontal plane through the cylindrical drying zone, thereby providing that practically each of the sprays disintegrates into particles inside said cylindrical drying zone, whereby the only disintegrated particles Penetrating low pressure vortex tubes are those that are incidentally transported by the cyclonic movement of the drying gas. (Machine-translation by Google Translate, not legally binding)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US60011A US3629951A (en) | 1970-07-31 | 1970-07-31 | Multilevel spray-drying method |
US60012A US3629955A (en) | 1970-07-31 | 1970-07-31 | Multilevel spray-drying apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
ES393643A1 true ES393643A1 (en) | 1974-06-01 |
Family
ID=26739457
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES393643A Expired ES393643A1 (en) | 1970-07-31 | 1971-07-26 | Multi-level spray drying method |
Country Status (13)
Country | Link |
---|---|
JP (1) | JPS534257B1 (en) |
AT (1) | AT325752B (en) |
AU (1) | AU459045B2 (en) |
BE (1) | BE770738A (en) |
CA (1) | CA938880A (en) |
CH (1) | CH575995A5 (en) |
DE (1) | DE2138087B2 (en) |
ES (1) | ES393643A1 (en) |
FR (1) | FR2099409A5 (en) |
GB (1) | GB1315882A (en) |
NL (1) | NL167992B (en) |
PH (2) | PH10273A (en) |
SE (1) | SE391535B (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5254709A (en) * | 1975-10-31 | 1977-05-04 | Lion Corp | Multi-stage spray drying method |
AU570738B2 (en) * | 1983-10-26 | 1988-03-24 | Unilever Plc | Detergent powder |
US20030203832A1 (en) * | 2002-04-26 | 2003-10-30 | The Procter & Gamble Company | Low organic spray drying process and composition formed thereby |
CN104959087B (en) | 2010-04-09 | 2017-08-15 | 帕西拉制药有限公司 | For preparing the method that major diameter synthesizes membrane vesicle |
CN104548633B (en) * | 2014-12-18 | 2016-05-25 | 方萌 | A kind of high-efficiency circulation type evaporation equipment |
CN111023782A (en) * | 2019-12-20 | 2020-04-17 | 丹阳市逸帆电子有限公司 | Special high-efficient drying device of panel preparation moulds plastics |
CN111957058B (en) * | 2020-08-31 | 2023-08-15 | 江苏瑞升华能源科技有限公司 | Spray drying device and process for salt-containing mother liquor |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1985987A (en) * | 1932-07-29 | 1935-01-01 | Procter & Gamble | Art of spray drying soap |
BE507042A (en) * | 1950-11-10 | |||
US2891611A (en) * | 1955-03-11 | 1959-06-23 | Colgate Palmolive Co | Spray drying apparatus |
FR1186591A (en) * | 1957-11-20 | 1959-08-27 | Spray Dryer Improvements | |
GB1059471A (en) * | 1963-06-04 | 1967-02-22 | Schuchtermann & Kremer Baum Ag | Method and apparatus for heat exchange, more particularly for the drying of solids suspended in a gas stream and known as suspension drying |
DE1262908B (en) * | 1964-04-28 | 1968-03-07 | Uta Patentverwaltungs G M B H | Drying tower with dust dusters in the upper area and brushing system for the tower walls |
GB1189543A (en) * | 1967-07-19 | 1970-04-29 | Colgate Palmolive Co | Process and Apparatus for Producing a Particulate Product |
DK124222B (en) * | 1968-07-09 | 1972-09-25 | Niro Atomizer As | Atomizer dryer. |
US3519054A (en) * | 1969-01-06 | 1970-07-07 | Colgate Palmolive Co | Process for producing a particulate product |
-
1971
- 1971-07-26 ES ES393643A patent/ES393643A1/en not_active Expired
- 1971-07-26 SE SE7109570A patent/SE391535B/en unknown
- 1971-07-28 CA CA119317A patent/CA938880A/en not_active Expired
- 1971-07-29 CH CH1119571A patent/CH575995A5/xx not_active IP Right Cessation
- 1971-07-30 AT AT668771A patent/AT325752B/en not_active IP Right Cessation
- 1971-07-30 NL NL7110551.A patent/NL167992B/en not_active Application Discontinuation
- 1971-07-30 BE BE770738A patent/BE770738A/en unknown
- 1971-07-30 GB GB3594371A patent/GB1315882A/en not_active Expired
- 1971-07-30 DE DE2138087A patent/DE2138087B2/en not_active Ceased
- 1971-07-30 FR FR7128136A patent/FR2099409A5/fr not_active Expired
- 1971-07-31 JP JP5787471A patent/JPS534257B1/ja active Pending
- 1971-08-02 PH PH12712A patent/PH10273A/en unknown
- 1971-08-02 AU AU31905/71A patent/AU459045B2/en not_active Expired
-
1976
- 1976-06-18 PH PH18585A patent/PH15337A/en unknown
Also Published As
Publication number | Publication date |
---|---|
JPS534257B1 (en) | 1978-02-15 |
BE770738A (en) | 1971-12-01 |
CH575995A5 (en) | 1976-05-31 |
AU459045B2 (en) | 1975-03-13 |
DE2138087A1 (en) | 1972-02-10 |
PH15337A (en) | 1982-11-24 |
ATA668771A (en) | 1975-01-15 |
GB1315882A (en) | 1973-05-02 |
DE2138087B2 (en) | 1980-09-18 |
AT325752B (en) | 1975-11-10 |
SE391535B (en) | 1977-02-21 |
FR2099409A5 (en) | 1972-03-10 |
PH10273A (en) | 1976-11-03 |
NL7110551A (en) | 1972-02-02 |
CA938880A (en) | 1973-12-25 |
NL167992B (en) | 1981-09-16 |
AU3190571A (en) | 1973-02-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
GB1350098A (en) | Spray drying | |
GB962265A (en) | Improvements in the granulating and drying of fluid materials such as aqueous solutions, pastes and slurries | |
US4051603A (en) | Fluidized bed apparatus | |
GB1153706A (en) | Apparatus for Granulation and Drying Fluid Substances | |
GB1279799A (en) | Improvements in or relating to blending apparatus | |
US3152005A (en) | Process for the preparation of pelletized solids | |
US3842888A (en) | Apparatus for introducing ingredients into a spray drying tower | |
ES393643A1 (en) | Multi-level spray drying method | |
ES197008U (en) | Apparatus for preferably electrostatic coating, of objects with pulverulent substances. (Machine-translation by Google Translate, not legally binding) | |
US1601898A (en) | Granular product and method of producing same | |
GB1524845A (en) | Spray dryer | |
GB845041A (en) | Carbon black pelleting process and apparatus | |
US3794099A (en) | Fluidized bed process for drying ammonium sulphate | |
US3471263A (en) | Mixing arrangement | |
US3793740A (en) | Fluidized bed process | |
GB1223646A (en) | Continuous process for surface drying granular materials and apparatus for carrying out such process | |
GB1081739A (en) | Disposal of waste liquors and recovery of inorganic chemicals therefrom | |
JPS5556801A (en) | Spray drying apparatus | |
GB1026329A (en) | Preparation of pelletized solid materials | |
GB1406879A (en) | Method of absorbing waste gases containing nitrogen oxides | |
GB1283122A (en) | Improvements in and relating to process for producing cement from cement slurry and a plant for carrying out the process | |
JPS54159417A (en) | Preparation of particulate detergent | |
GB1325224A (en) | Fluidised beds | |
GB837398A (en) | Improvements in or relating to the quenching of hot coke | |
JPS5424299A (en) | Production of hydrated sodium silicate of high bulk density |