AT14899B - Process for the constant diffusion or leaching of beet pulp, bagasse, colored wood or tanning wood and the like. like - Google Patents
Process for the constant diffusion or leaching of beet pulp, bagasse, colored wood or tanning wood and the like. likeInfo
- Publication number
- AT14899B AT14899B AT14899DA AT14899B AT 14899 B AT14899 B AT 14899B AT 14899D A AT14899D A AT 14899DA AT 14899 B AT14899 B AT 14899B
- Authority
- AT
- Austria
- Prior art keywords
- wood
- bagasse
- leaching
- tanning
- beet pulp
- Prior art date
Links
- 238000002386 leaching Methods 0.000 title claims description 3
- 238000000034 method Methods 0.000 title claims 2
- 241000609240 Ambelania acida Species 0.000 title description 4
- 239000010905 bagasse Substances 0.000 title description 4
- 239000002023 wood Substances 0.000 title description 4
- 241000335053 Beta vulgaris Species 0.000 title description 2
- 238000009792 diffusion process Methods 0.000 title description 2
- 235000016068 Berberis vulgaris Nutrition 0.000 title 1
- 239000000463 material Substances 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 6
- 238000006073 displacement reaction Methods 0.000 description 2
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Paper (AREA)
Description
<Desc/Clms Page number 1>
EMI1.1
EMI1.2
EMI1.3
<Desc/Clms Page number 2>
EMI2.1
EMI2.2
<Desc/Clms Page number 3>
EMI3.1
<Desc/Clms Page number 4>
EMI4.1
<Desc/Clms Page number 5>
EMI5.1
Gefäss D unterdessen auf der gewünschten Hure, also bei X.
Wie oben ausgeführt, genügt in der Regel Luftleere allein, d. h. absoluter Druck
EMI5.2
kann nur bei einigen sehr voluminösen Materialien der Fall soin, welche in ihrer Schichtung sehr viele lileine bezw. iin anderen Falle relativ grosse Zwichenräl1mc bilden und so den Druckströmen der Flüssigkeiten wenig Widerstand entgegensetzen.
In den Fällen nun, wo aus ziemlich voluminösen Materialien ein konzentrierter Saft gewonnen werden soll, muss das Verhältnis der Menge dieses Materials zur Flüssigkeitsmenge günstiger gestaltet werden ; zu dem Zwecke bleiben, wie soeben ausgeführt, die (durch Pressung durch Schnecke B) ohnehin verringerten Zwischenräume der Bagasse nicht in der ganzen Lünge des Gefässes D mit Verdrängungsflüssigkeit gefüllt, z. B. von der Stelle X bis zum Mantel k1, so dass vom Mantel G1 ab bis zur Stelle X die in den
EMI5.3
von Bagasse gedrückt.
Um nun aber den erforderlichen Druck zu schaffen, müssen die von Flüssigkeit freibleibenden Zwischenräume vom Mantel G1 bis zur Stelle X durch ein Gas unter höherem als Atmosphärendruck 8usgefttllt werden ; es sind dafür geeignet Dampf von geringer Spannung, komprimierte Luft.
Das mit dem Dampf zugleich - dann natürlich heisse - Wasser kann in den mit Dampf gefüllten Zwischenräumen herabsickern, wenn es die Temperatur des Dampfes an genommen hat.
EMI5.4
wärtigen muss.
EMI5.5
<Desc/Clms Page number 6>
RaumundKostenersparnis, Leichtere, einfachere und billigere Bedienung,
EMI6.1
Wiederverwendung der Süsswasser.
Bessere Ausnutzung der Wärme und Brennmaterialersparnis, da konzentriertere Säfte gewonnen werden.
EMI6.2
das zu behandelnde Material, z. B. Rübenschnitzol, Bagasse, zerkleinertes Farbholz, Gerbholz oder dgl., mechanisch der Verdrängung-, bezw. Auslaugungsflüssigkeit entgegenbewegt wird, wobei der Diffusionsprozess in der gleichmassig kompakt geschichteten Masse innerhalb eines von Förder- und Heizvorrichtungne freien Diffuseurs unter Luftleere beginnt und im weiteren Verlauf unter Druck vor sich geht.
<Desc / Clms Page number 1>
EMI1.1
EMI1.2
EMI1.3
<Desc / Clms Page number 2>
EMI2.1
EMI2.2
<Desc / Clms Page number 3>
EMI3.1
<Desc / Clms Page number 4>
EMI4.1
<Desc / Clms Page number 5>
EMI5.1
Vessel D meanwhile on the desired whore, i.e. at X.
As stated above, evacuation alone is usually sufficient, i. H. absolute pressure
EMI5.2
can only be the case with some very voluminous materials, which in their layering have a lot of purple lines or In other cases they form relatively large spaces and thus offer little resistance to the pressure currents of the liquids.
In those cases where a concentrated juice is to be obtained from fairly voluminous materials, the ratio of the amount of this material to the amount of liquid must be made more favorable; For this purpose, as just stated, the gaps between the bagasse, which are already reduced (by pressing by screw B), are not filled with displacement liquid over the entire length of the vessel D, e.g. B. from the point X to the coat k1, so that from the coat G1 to the point X in the
EMI5.3
pressed by bagasse.
However, in order to create the required pressure, the spaces from the jacket G1 to the point X that remain free of liquid must be filled with a gas at a pressure higher than atmospheric pressure; low tension steam, compressed air, is suitable for this.
The water at the same time as the steam - then naturally hot - can seep down into the spaces filled with steam when it has reached the temperature of the steam.
EMI5.4
must wait.
EMI5.5
<Desc / Clms Page number 6>
Space and cost savings, easier, simpler and cheaper operation,
EMI6.1
Reuse the fresh water.
Better utilization of heat and fuel savings, as more concentrated juices are obtained.
EMI6.2
the material to be treated, e.g. B. beet pulp, bagasse, crushed colored wood, tanning wood or the like., Mechanically the displacement, respectively. Leaching liquid is moved in the opposite direction, the diffusion process beginning in the uniformly compact layered mass within a diffuser free of conveying and heating devices, under a vacuum, and continuing under pressure.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE1900135880D DE135880C (en) | 1900-11-08 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AT14899B true AT14899B (en) | 1904-01-25 |
Family
ID=5666150
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AT14899D AT14899B (en) | 1900-11-08 | 1902-11-28 | Process for the constant diffusion or leaching of beet pulp, bagasse, colored wood or tanning wood and the like. like |
Country Status (1)
| Country | Link |
|---|---|
| AT (1) | AT14899B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE938599C (en) * | 1952-08-17 | 1956-02-02 | Buckau Wolf Maschf R | Diffusion process, especially for beet pulp |
-
1902
- 1902-11-28 AT AT14899D patent/AT14899B/en active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE938599C (en) * | 1952-08-17 | 1956-02-02 | Buckau Wolf Maschf R | Diffusion process, especially for beet pulp |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| DE1567598B1 (en) | Process for the production of a profiled hydrogen permeable membrane | |
| DE3122186C2 (en) | ||
| DE69009405T2 (en) | Separation of gas mixtures. | |
| DE19922310B4 (en) | Pressure-resistant container for the preservation of tissues and organs | |
| DE1252633B (en) | Device for separating pure gases by diffusion | |
| AT14899B (en) | Process for the constant diffusion or leaching of beet pulp, bagasse, colored wood or tanning wood and the like. like | |
| DE1957604A1 (en) | Method and device for hot-pressing sheets made from lignocellulosic materials | |
| CH410788A (en) | Process for the multi-stage drying of filtration residues in disc filters | |
| DE2050917B2 (en) | PROCESS AND DEVICE FOR DEACUIFICATION | |
| AT67672B (en) | Method of treating cork by means of heat. | |
| AT54627B (en) | Apparatus for concentrating liquids. | |
| DE22172C (en) | Process for cooling the blower wind in ironworks processes | |
| AT36221B (en) | Device for sterilizing liquids using ozone. | |
| AT77968B (en) | Method and device for draining peat soil. | |
| AT135655B (en) | Method for removing glue from goods containing glue. | |
| AT32863B (en) | Method and device for drying beet pulp and similar substances by indirect heating with steam in several drying stations. | |
| AT71146B (en) | Process for the continuous concentration of dilute nitric acid. | |
| DE135880C (en) | ||
| DE961857C (en) | Method and device for preventing the clogging of the heat exchanger by fibers during the circulation heating of the cooking liquid for pulp digesters | |
| AT42048B (en) | Process and device for continuous juice extraction. | |
| AT146893B (en) | Process for the production of briquettes. | |
| DE1467529C (en) | Process for the continuous hardening of unsaturated oils and fats | |
| AT21467B (en) | Process for extracting juice from sugar beets, sugar cane or other sugary plants by leaching. | |
| AT35659B (en) | Method and apparatus for dyeing, washing, bleaching and the like of textile fabrics. | |
| AT87236B (en) | Method for pressing plates, trays or other solid pieces of loose structure made of peat fibers and a fusible binding agent. |