GB759169A - Improvements in or relating to the continuous de-aeration of viscous spinning solutions - Google Patents
Improvements in or relating to the continuous de-aeration of viscous spinning solutionsInfo
- Publication number
- GB759169A GB759169A GB25763/53A GB2576353A GB759169A GB 759169 A GB759169 A GB 759169A GB 25763/53 A GB25763/53 A GB 25763/53A GB 2576353 A GB2576353 A GB 2576353A GB 759169 A GB759169 A GB 759169A
- Authority
- GB
- United Kingdom
- Prior art keywords
- pipe
- solution
- viscose
- deaerated
- vertical
- 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
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D1/00—Treatment of filament-forming or like material
- D01D1/10—Filtering or de-aerating the spinning solution or melt
- D01D1/103—De-aerating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0042—Degasification of liquids modifying the liquid flow
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F2/00—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
- D01F2/06—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof from viscose
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S159/00—Concentrating evaporators
- Y10S159/04—Foam
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S159/00—Concentrating evaporators
- Y10S159/31—Deaeration
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Textile Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Artificial Filaments (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
Abstract
<PICT:0759169/IV(a)/1> <PICT:0759169/IV(a)/2> Viscose spinning solutions for the manufacture of artificial threads and films are continuously deaerated by passing the solution upwardly through a vertical or nearly vertical pipe into a chamber which is maintained at a reduced pressure and from which the deaerated solution is finally discharged, the flow of solution up the pipe, the dimensions of the pipe, the supply of solution to the pipe and the reduced pressure together being so adjusted that, in an intermediate region of the pipe, the pressure on the solution is below the vapour pressure of the solution, the conditions in the pipe in and above said region being such that the bubbles, as they are formed, move upwards substantially at the same speed as the solution and the cooling of the solution as a result of boiling being such that, at the upper end of the pipe, boiling ceases. The vertical pipe may be provided with obstructions, e.g. sieves, to retard the rise of bubbles. The spinning solution may be preheated and specified solutions are, in addition to viscose and cuprammonium cellulose solutions, those of polyamides in benzene, polyacrylonitrile in dimethylformamide, cellulose acetate in acetone and copolymers of acrylonitrile in organic solvents. As shown (Fig. 1), viscose from a reservoir 1 flows through pipe 3, heater 4 and valve 5 to the vertical pipe 2, the upper end of which discharges into a chamber 10 maintained under reduced pressure. Air and gases are withdrawn at 11 and the deaerated viscose is discharged through pipe 6. In a modification (Fig. 2) viscose from heater 4 is fed through a pipe 7 with a narrowed end 8 into a concentric vertical pipe 2 provided with obstructions in the form of sieves 9.ALSO:<PICT:0759169/III/1> <PICT:0759169/III/2> Viscous spinning solutions for the manufacture of artificial threads and films are continuously deaerated by passing the solution upwardly through a vertical or nearly vertical pipe into a chamber which is maintained at a reduced pressure and from which the deaerated solution is finally discharged, the flow of solution up the pipe, the dimensions of the pipe, the supply of solution to the pipe and the reduced pressure together being so adjusted that, in an intermediate region of the pipe, the pressure on the solution is below the vapour pressure of the solution, the conditions in the pipe in and above said region being such that the bubbles, as they are formed, moved upwards substantially at the same speed as the solution and the cooling of the solution as a result of boiling being such that, at the upper end of the pipe, boiling ceases. The vertical pipe may be provided with obstructions, e.g. sieves, to retard the rise of bubbles. The spinning solution may be preheated, and specified solutions are those of viscose, cuprammonium cellulose, polyamides, polyacrylonitrile and cellulose acetate. As shown (Fig. 1), viscose from a reservoir 1 flows through pipe 3, heater 4 and valve 5 to the vertical pipe 2, the upper end of which discharges into a chamber 10 maintained under reduced pressure. Air and gases are withdrawn at 11 and the deaerated viscose is discharged through pipe 6. In a modification (Fig. 2), viscose from heater 4 is fed through a pipe 7 with a narrowed end 8 into a concentric vertical pipe 2 provided with obstructions in the form of sieves 9.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL759169X | 1953-02-09 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB759169A true GB759169A (en) | 1956-10-17 |
Family
ID=19825365
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB25763/53A Expired GB759169A (en) | 1953-02-09 | 1953-09-17 | Improvements in or relating to the continuous de-aeration of viscous spinning solutions |
Country Status (5)
Country | Link |
---|---|
US (1) | US2774441A (en) |
BE (1) | BE522463A (en) |
DE (1) | DE1089113B (en) |
GB (1) | GB759169A (en) |
NL (2) | NL77351C (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL243909A (en) * | 1958-12-23 | |||
DE1197846B (en) * | 1961-03-16 | 1965-08-05 | Daimler Benz Ag | Method and device for degassing liquids or melts |
BE615380A (en) * | 1961-03-22 | |||
DE1302684B (en) * | 1961-06-21 | 1971-04-01 | Automatic Process Control Inc | |
US3793805A (en) * | 1971-12-13 | 1974-02-26 | Eastman Kodak Co | Method and apparatus for removing air from a liquid |
DE102016116989A1 (en) * | 2016-09-09 | 2018-03-15 | Endress+Hauser Flowtec Ag | Gas separator and device for determining a flow of one or more components of a multiphase medium, in particular a natural gas-water mixture. |
CN115522265A (en) * | 2022-05-24 | 2022-12-27 | 崔文斌 | Chemical fiber silk pretreatment equipment for chemical fiber cloth manufacturing |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE389698C (en) * | 1924-02-06 | Schmidt Sche Heissdampf Ges M | Process for cleaning preheated boiler feed water from gaseous admixtures | |
US863031A (en) * | 1907-08-13 | Fischer Ernst | Apparatus for treating foaming liquids. | |
US414618A (en) * | 1889-11-05 | Serei | ||
US1529884A (en) * | 1925-03-17 | Apparatus por deaeration op liquids | ||
US847085A (en) * | 1906-06-23 | 1907-03-12 | Fischer Ernst | Apparatus for treating foaming liquids. |
US1581371A (en) * | 1925-02-04 | 1926-04-20 | Edwin C Weisgerber | Gas and oil separator |
US2006985A (en) * | 1926-03-13 | 1935-07-02 | Claude George | Method and apparatus for obtaining power from sea water |
US1926191A (en) * | 1926-10-15 | 1933-09-12 | Boucherot Paul | Treatment of quantities of water |
US1752215A (en) * | 1928-04-09 | 1930-03-25 | Smith Separator Company | Oil and gas separator |
DE734028C (en) * | 1935-06-21 | 1943-04-07 | Kraftanlagen Ag | Degassing system |
US2355057A (en) * | 1941-07-18 | 1944-08-08 | Du Pont | Apparatus for deaerating viscose compositions |
-
0
- NL NLAANVRAGE7500305,A patent/NL175919B/en unknown
- BE BE522463D patent/BE522463A/xx unknown
- NL NL77351D patent/NL77351C/xx active
-
1953
- 1953-08-31 DE DEN7670A patent/DE1089113B/en active Pending
- 1953-09-17 GB GB25763/53A patent/GB759169A/en not_active Expired
- 1953-11-30 US US395161A patent/US2774441A/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
BE522463A (en) | |
NL175919B (en) | |
DE1089113B (en) | 1960-09-15 |
US2774441A (en) | 1956-12-18 |
NL77351C (en) |
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