BE445567A - - Google Patents
Info
- Publication number
- BE445567A BE445567A BE445567DA BE445567A BE 445567 A BE445567 A BE 445567A BE 445567D A BE445567D A BE 445567DA BE 445567 A BE445567 A BE 445567A
- Authority
- BE
- Belgium
- Prior art keywords
- bath
- gas
- emi
- devices
- absorption
- Prior art date
Links
- 239000007789 gas Substances 0.000 claims description 11
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 claims description 8
- 239000007788 liquid Substances 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 5
- 238000001556 precipitation Methods 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 238000010521 absorption reaction Methods 0.000 claims description 4
- 238000005273 aeration Methods 0.000 claims description 3
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims description 2
- 238000009833 condensation Methods 0.000 claims description 2
- 230000005494 condensation Effects 0.000 claims description 2
- 238000001035 drying Methods 0.000 claims description 2
- 229910000037 hydrogen sulfide Inorganic materials 0.000 claims description 2
- 239000011261 inert gas Substances 0.000 claims description 2
- 238000001179 sorption measurement Methods 0.000 claims 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 2
- 150000003464 sulfur compounds Chemical class 0.000 claims 2
- 239000004215 Carbon black (E152) Substances 0.000 claims 1
- 238000004821 distillation Methods 0.000 claims 1
- 229930195733 hydrocarbon Natural products 0.000 claims 1
- 150000002430 hydrocarbons Chemical class 0.000 claims 1
- 238000002347 injection Methods 0.000 claims 1
- 239000007924 injection Substances 0.000 claims 1
- 238000011084 recovery Methods 0.000 claims 1
- 239000003507 refrigerant Substances 0.000 claims 1
- 238000003756 stirring Methods 0.000 claims 1
- 229920000297 Rayon Polymers 0.000 description 2
- 229920002678 cellulose Polymers 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- 230000008929 regeneration Effects 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229920002955 Art silk Polymers 0.000 description 1
- 240000000491 Corchorus aestuans Species 0.000 description 1
- 235000011777 Corchorus aestuans Nutrition 0.000 description 1
- 235000010862 Corchorus capsularis Nutrition 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 210000002268 wool Anatomy 0.000 description 1
Classifications
-
- 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
- D01F13/00—Recovery of starting material, waste material or solvents during the manufacture of artificial filaments or the like
- D01F13/02—Recovery of starting material, waste material or solvents during the manufacture of artificial filaments or the like of cellulose, cellulose derivatives or proteins
-
- 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
- Y02P70/62—Manufacturing or production processes characterised by the final manufactured product related technologies for production or treatment of textile or flexible materials or products thereof, including footwear
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Drying Of Gases (AREA)
Description
Procédé d'aération des bains de précipitation dans les fabrications de viscose.
Dans les fabriques de soie artificielles, de jute de cellulose, de feuilles plastiques cellulosiques, de laine
<EMI ID=1.1>
se, le bain de précipitation, lors du pressage de la viscose est continuellement étendu d'eau et en même temps enrichi
en substances de valeur, mais insalubres comme l'hydrogène sulfuré et le sulfure de carbone. En conséquence le problème se pose de débarrasser le bain de l'eau en excès et de récupérer les substances de valeur qui y ont été introduites.
<EMI ID=2.1>
temps à autre dans la cuve de travail une partie du liquide du bain, en le régénérant et en le réintroduisant ensuite dans la cuve. La régénération s'effectue en séparant l'eau
<EMI ID=3.1>
cupérer le sulfure de carbone par vaporisation dans le vide suivie de condensation. Ce procédé se heurte à des difficultés de tous genres qui entraînent des installations compliquées. En outre et surtout il a l'inconvénient d'avoir besoin d'un excès de bain de précipitation en vue de compenser les pré-
<EMI ID=4.1>
et par suite d'obliger à tenir compte de variations continuelles dans la concentration du bain de travail.
Le procédé de l'invention réunit l'ensemble des opérations de régénération en un unique processus continu, il simplifie les moyens à mettre en oeuvre, économise une grande partie du liquide du bain de précipitation jusqu'ici
<EMI ID=5.1>
sous vide, à introduire dans le bain, par en bas, de l'air ou un autre gaz iherte, à le réaspirer par en haut, à le diriger dans des appareils d'absorption et de séchage, puis à le réintroduire dans le bain, en le faisant ainsi circuler en circuit fermé.
Ce procédé est mis en oeuvre de la façon suivante :
l'air ou le gaz inerte est introduit dans le bain à l'état chaud, il y est insufflé, par exemple à travers un filtre céramique, de façon à obtenir un courant gazeux finement divisé. Pour assurer une répartition uniforme du gaz dans le
Aeration process for precipitation baths in viscose manufacturing.
In the factories of artificial silk, cellulose jute, cellulose plastic sheets, wool
<EMI ID = 1.1>
se, the precipitation bath, when pressing the viscose is continuously diluted with water and at the same time enriched
valuable but unsanitary substances like hydrogen sulfide and carbon disulphide. Consequently the problem arises of ridding the bath of excess water and of recovering the valuable substances which have been introduced therein.
<EMI ID = 2.1>
from time to time in the working tank a part of the liquid of the bath, regenerating it and then reintroducing it into the tank. Regeneration is carried out by separating the water
<EMI ID = 3.1>
cuper the carbon disulphide by vaporization in a vacuum followed by condensation. This process comes up against all kinds of difficulties which lead to complicated installations. In addition and above all, it has the drawback of needing an excess of precipitation bath in order to compensate for the pre-
<EMI ID = 4.1>
and consequently to oblige to take account of continual variations in the concentration of the working bath.
The method of the invention combines all the regeneration operations into a single continuous process, it simplifies the means to be implemented, saves a large part of the liquid in the precipitation bath so far.
<EMI ID = 5.1>
vacuum, to introduce into the bath, from below, air or another iherte gas, to suck it again from above, to direct it into absorption and drying devices, then to reintroduce it into the bath , thus making it circulate in a closed circuit.
This process is implemented as follows:
the air or the inert gas is introduced into the bath in the hot state, it is blown therein, for example through a ceramic filter, so as to obtain a finely divided gas stream. To ensure even distribution of gas in the
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE228895X | 1941-05-15 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| BE445567A true BE445567A (en) |
Family
ID=5867469
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| BE445567D BE445567A (en) | 1941-05-15 |
Country Status (3)
| Country | Link |
|---|---|
| BE (1) | BE445567A (en) |
| CH (1) | CH228895A (en) |
| FR (1) | FR881863A (en) |
-
0
- BE BE445567D patent/BE445567A/fr unknown
-
1942
- 1942-03-23 CH CH228895D patent/CH228895A/en unknown
- 1942-05-08 FR FR881863D patent/FR881863A/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| CH228895A (en) | 1943-09-30 |
| FR881863A (en) | 1943-05-11 |
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