DE1592994C - Process for the extraction of oil or fat from sewage - Google Patents
Process for the extraction of oil or fat from sewageInfo
- Publication number
- DE1592994C DE1592994C DE19661592994 DE1592994A DE1592994C DE 1592994 C DE1592994 C DE 1592994C DE 19661592994 DE19661592994 DE 19661592994 DE 1592994 A DE1592994 A DE 1592994A DE 1592994 C DE1592994 C DE 1592994C
- Authority
- DE
- Germany
- Prior art keywords
- water
- oil
- acid
- glue
- separation
- 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
- 238000000605 extraction Methods 0.000 title claims 5
- 238000000034 method Methods 0.000 title claims 2
- 239000010865 sewage Substances 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 40
- 238000005119 centrifugation Methods 0.000 claims description 13
- 239000003292 glue Substances 0.000 claims description 12
- 239000002253 acid Substances 0.000 claims description 11
- 239000002351 wastewater Substances 0.000 claims description 11
- 238000000926 separation method Methods 0.000 claims description 10
- 102000004169 proteins and genes Human genes 0.000 claims description 9
- 108090000623 proteins and genes Proteins 0.000 claims description 9
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 8
- 235000019749 Dry matter Nutrition 0.000 claims description 6
- 238000005188 flotation Methods 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 5
- 235000019733 Fish meal Nutrition 0.000 claims description 4
- 239000004467 fishmeal Substances 0.000 claims description 4
- 238000004458 analytical method Methods 0.000 claims description 3
- 235000019514 herring Nutrition 0.000 claims description 3
- 239000000839 emulsion Substances 0.000 claims description 2
- 150000002484 inorganic compounds Chemical class 0.000 claims description 2
- 229910010272 inorganic material Inorganic materials 0.000 claims description 2
- 239000003921 oil Substances 0.000 claims 22
- 239000003925 fat Substances 0.000 claims 5
- 229920005610 lignin Polymers 0.000 claims 2
- 239000000463 material Substances 0.000 claims 2
- 230000001105 regulatory Effects 0.000 claims 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-N sulfonic acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 claims 2
- 241000251468 Actinopterygii Species 0.000 claims 1
- 241001454694 Clupeiformes Species 0.000 claims 1
- 235000001211 Talinum portulacifolium Nutrition 0.000 claims 1
- 240000004958 Talinum portulacifolium Species 0.000 claims 1
- 210000001138 Tears Anatomy 0.000 claims 1
- 229940029983 VITAMINS Drugs 0.000 claims 1
- 229940021016 Vitamin IV solution additives Drugs 0.000 claims 1
- 210000002268 Wool Anatomy 0.000 claims 1
- 230000000903 blocking Effects 0.000 claims 1
- 238000004140 cleaning Methods 0.000 claims 1
- 235000013365 dairy product Nutrition 0.000 claims 1
- 235000019688 fish Nutrition 0.000 claims 1
- PEDCQBHIVMGVHV-UHFFFAOYSA-N glycerine Chemical class OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims 1
- 235000012054 meals Nutrition 0.000 claims 1
- 239000007764 o/w emulsion Substances 0.000 claims 1
- 235000014593 oils and fats Nutrition 0.000 claims 1
- 150000002894 organic compounds Chemical class 0.000 claims 1
- 239000005416 organic matter Substances 0.000 claims 1
- 230000036284 oxygen consumption Effects 0.000 claims 1
- 239000002245 particle Substances 0.000 claims 1
- 238000002360 preparation method Methods 0.000 claims 1
- 235000003441 saturated fatty acids Nutrition 0.000 claims 1
- 150000004671 saturated fatty acids Chemical class 0.000 claims 1
- 238000007790 scraping Methods 0.000 claims 1
- 235000002639 sodium chloride Nutrition 0.000 claims 1
- 239000011780 sodium chloride Substances 0.000 claims 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims 1
- 239000011343 solid material Substances 0.000 claims 1
- 235000021122 unsaturated fatty acids Nutrition 0.000 claims 1
- 150000004670 unsaturated fatty acids Chemical class 0.000 claims 1
- 235000013343 vitamin Nutrition 0.000 claims 1
- 239000011782 vitamin Substances 0.000 claims 1
- 229930003231 vitamins Natural products 0.000 claims 1
- 238000003911 water pollution Methods 0.000 claims 1
- 239000000654 additive Substances 0.000 description 6
- 230000000996 additive Effects 0.000 description 4
- 241000252203 Clupea harengus Species 0.000 description 2
- YDEXUEFDPVHGHE-GGMCWBHBSA-L disodium;(2R)-3-(2-hydroxy-3-methoxyphenyl)-2-[2-methoxy-4-(3-sulfonatopropyl)phenoxy]propane-1-sulfonate Chemical compound [Na+].[Na+].COC1=CC=CC(C[C@H](CS([O-])(=O)=O)OC=2C(=CC(CCCS([O-])(=O)=O)=CC=2)OC)=C1O YDEXUEFDPVHGHE-GGMCWBHBSA-L 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- WPWCLBXYKATSMD-UHFFFAOYSA-N [2-(tert-butylcarbamoylamino)-2-oxoethyl] 3-cyclopentylpropanoate Chemical compound CC(C)(C)NC(=O)NC(=O)COC(=O)CCC1CCCC1 WPWCLBXYKATSMD-UHFFFAOYSA-N 0.000 description 1
- 235000012970 cakes Nutrition 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000010297 mechanical methods and process Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- KEAYESYHFKHZAL-UHFFFAOYSA-N sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
Description
an Hand eines pH-Meters auf 3,0 eingestellt. Durch diesen Ligninsulfonsäurezusatz wurde die Emulsion gebrochen.adjusted to 3.0 using a pH meter. This addition of lignosulfonic acid made the emulsion Broken.
Von der Rohrleitung wurde das derart behandelte Leimwasser in einen 350 1 großen Behälter geleitet und von diesem in eine andere Zentrifuge. In dieser wurde durch die Zentrifugierung pro Kubikmeter behandeltes LeimwasserThe glue water treated in this way was passed from the pipeline into a 350 l container and from this to another centrifuge. In this was by centrifugation per cubic meter treated glue water
210 kg Schlamm, enthaltend
69 kg Trockensubstanz, wovonContaining 210 kg of sludge
69 kg dry matter, of which
9 kg Ligninsulfonsäure,
55 kg Proteine und9 kg lignosulfonic acid,
55 kg of proteins and
5 kg andere Stoffe sind,5 kg are other substances,
ausgeschieden.eliminated.
Außerdem wurden von der Zentrifuge 11 kg = etwa 12 1 öl separat ausgeschieden. Das von der Zentrifuge abgehende Wasser hatte folgende Analyse:In addition, the centrifuge weighed 11 kg = about 12 1 oil excreted separately. The water leaving the centrifuge had the following analysis:
Trockensubstanz 2,8%Dry matter 2.8%
HiervonOf this
Proteine 0,5%Proteins 0.5%
anorganische Verbindungen .... 1,8%inorganic compounds .... 1.8%
ül 0,3%ül 0.3%
sonstige 0,2%other 0.2%
Das öl (sowohl von der ersten als auch zweiten Zentrifugierung) wurde zur Raffinierung gesandt und der Schlamm in einem Trockner zusammen mit dem Preßkuchen der Fischmehlfabrik getrocknet.The oil (from both the first and second centrifugations) was sent for refining and the sludge is dried in a dryer together with the press cake from the fishmeal factory.
Es ist zu bemerken, daß die angeführten Analysen Durchschnittsanalysen einer 8stündigen Tätigkeit sind, in welcher Periode die Anlage von insgesamt 15,3 m3 Leimwasser passiert wurde.It should be noted that the analyzes cited are average analyzes of an 8-hour activity, in which period a total of 15.3 m 3 of glue water was passed through the system.
Wenn im oben Angeführten Zentrifugierung als Trennmethode angegeben ist, so ist hiermit zu verstehen, daß auch andere, auf dem Gebiete mechanischer Verfahren bekannte Trennmethoden angewandt werden können.If centrifugation is specified as the separation method in the above, this is to be understood as that other separation methods known in the field of mechanical processes are also used can be.
Abwasser aus einer Heringsfiletanlage wurde einer Zentrifugierung mit und ohne Zusatz von Ligninsulfonsäure unterworfen. Das Wasser wurde vor und nach der Behandlung analysiert, die auf Durchschnittsproben basiert, welche derart genommen wurden, daß Wasser vor und nach der Zentrifugierung jede halbe Stunde über eine Zeitspanne von 5 Stunden in beiden Fällen ausgenommen wurde. In jeder Periode passierten 134 m3 Wasser. In dem Falle, in dem Ligninsulfonsäure zugesetzt wurde, wurden 68 kg reine Natrium-Ligninsulfonsäure und 60 kg Schwefelsäure angewandt. Waste water from a herring fillet plant was subjected to centrifugation with and without the addition of ligninsulphonic acid. The water before and after the treatment was analyzed based on average samples taken such that water before and after centrifugation was removed every half hour for a period of 5 hours in both cases. In each period, 134 m 3 of water passed. In the case where lignosulfonic acid was added, 68 kg of pure sodium ligninsulfonic acid and 60 kg of sulfuric acid were used.
AnalyseergebnisseAnalysis results
Trockenstoff, %Dry matter,%
Protein, % Protein,%
öl, % oil,%
Wasser bei
Zentrifugierung Water at
Centrifugation
1,55
0,76
0,761.55
0.76
0.76
Wasser nach Zentrifugierung ohne Zusatz mit ZusatzWater after centrifugation without additives with additives
1,03 0,70 0,241.03 0.70 0.24
0,82 0,36 0,060.82 0.36 0.06
Dies bedeutet, daß der ölseparierungseffekt war: ohne Zusatz:This means that the oil separation effect was: without addition:
0,52
0,760.52
0.76
3030th
35 mit Zusatz:35 with addition:
0,70
0,760.70
0.76
x 100 = 68% ,x 100 = 68%,
x 100 = 92% .x 100 = 92%.
2 x 9 m3 Wasser von einer Heringsfiletfabrik wurden Flotation unterworfen, indem dem einen Anteil vorher 8 kg Natriumligninsulfonsäure und 6 kg Schwefelsäure zugesetzt wurden. Nach der Flotation wurde die oberste Schicht abgeschabt und nach Erwärmung auf 8O0C zentrifugiert. Das gereinigte Wasser wurde nach der Flotation und Zentrifugierung in die beiden Fälle analysiert:2 × 9 m 3 of water from a herring fillet factory were subjected to flotation by adding 8 kg of sodium lignosulfonic acid and 6 kg of sulfuric acid to one portion beforehand. After flotation, the top layer was scraped off and centrifuged after heating at 8O 0 C. The purified water was analyzed in the two cases after flotation and centrifugation:
Wasser vor FlotationWater before flotation
Wasser nach Flotation mit Zusatz ohne ZusatzWater after flotation with additive without additive
Wasser nach Zentrifugierung mit Zusatz ohne ZusatzWater after centrifugation with additive without additive
Trockenstoff, %.Dry matter,%.
Protein, % Protein, %
öl, % oil,%
1,58
0,81
0,561.58
0.81
0.56
1,02
0,57
0,081.02
0.57
0.08
0,13
0,06
0,090.13
0.06
0.09
0,60 0,60 0,140.60 0.60 0.14
2 χ 20 1 Abwasser wurden von einer Schlächterei ausgenommen. Demeinen Anteil wurden 8 g Natriumligninsulfonsäure und 5 g konz. H2SO4 zugesetzt. Beide Anteile wurden bei Zimmertemperatur in2 χ 20 1 wastewater was exempted from a slaughterhouse. 8 g of sodium lignosulfonic acid and 5 g of conc. H 2 SO 4 added. Both portions were in
60 Trockenstoff, % 60 dry matter,%
2 Stunden stehengelassen, wobei sich ein Schaum auf der Oberfläche bildete und ein Teil als Ausfällung Fett, % sedimentierte. Das relativ klare Wasser in der MitteLeft to stand for 2 hours, during which a foam formed on the surface and part of it sedimented as a precipitate,% fat. The relatively clear water in the middle
und das Ausgangswasser wurden analysiert: Protein. %and the starting water were analyzed: protein. %
Un-U.N-
behandeltes
Wassertreated
water
0,62
0,18
0,250.62
0.18
0.25
Wasserwater
stehendstanding
mit Zusatzwith addition
0,12 0,04 0,040.12 0.04 0.04
In 2 Stunden ohne ZusatzIn 2 hours without any additions
0,35 0,10. 0,200.35 0.10. 0.20
Claims (3)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DK538465 | 1965-10-21 | ||
DK538465 | 1965-10-21 | ||
DEA0053862 | 1966-10-21 |
Publications (3)
Publication Number | Publication Date |
---|---|
DE1592994A1 DE1592994A1 (en) | 1971-02-11 |
DE1592994B2 DE1592994B2 (en) | 1973-01-04 |
DE1592994C true DE1592994C (en) | 1973-08-09 |
Family
ID=
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE2609705C3 (en) | Process for degumming triglyceride oils | |
EP0473985B1 (en) | Process for degumming | |
DE2740752C3 (en) | Process for removing contaminants from crude or pretreated triglyceride oil | |
DE2346494C2 (en) | Process for removing water from a mixture containing water and water-insoluble, finely divided solid material | |
DE69200004T2 (en) | METHOD FOR CONTINUOUSLY DEFLUATING A GLYCERIDOEL. | |
DE2719507C3 (en) | Process for cleaning waste water containing fat and earth with a solvent | |
DE69202792T2 (en) | Two-stage bleaching process for vegetable material. | |
DE3624205A1 (en) | METHOD FOR PRODUCING PHOSPHATID CONCENTRATES FROM PLANT OILS | |
DE815604C (en) | Process and device for the preparation of magnesium bisulphite liquor by absorbing SO from the combustion gases resulting from the calcination of the waste liquor | |
DE1592994C (en) | Process for the extraction of oil or fat from sewage | |
DE1592994B2 (en) | Process for the extraction of oil or fat from waste water | |
DE1617012C3 (en) | Process for obtaining lanolin from wastewater from wool laundry | |
DE3023589A1 (en) | METHOD FOR REFINING ANIMAL OR VEGETABLE OILS AND FATS | |
DE2522953C3 (en) | Process for the separation of non-volatile residual oil from dry solids | |
DE961282C (en) | Process for working up residues containing phosphatides and oil | |
DE940620C (en) | Process for making fish meal | |
DE3532737C2 (en) | ||
DE837910C (en) | Process for the production of oils or fats from vegetable or animal substances by extraction | |
DE2405874A1 (en) | PROCESS FOR RECOVERING AND STABILIZING FAT, FAT-LIKE SUBSTANCES, PROTEIN, PROTEIN-LIKE SUBSTANCES AND / OR DEGRADATION PRODUCTS OF THE ABOVE SUBSTANCES FROM USED WATER OR WASTE WATER | |
DE2025739C (en) | Process for degumming and alkali refining of raw glycendol | |
DE826752C (en) | Process for the production of surface-active substances which contain silica | |
DE2332668A1 (en) | METHOD OF EXTRACTION OF PROTEINS FROM ORGANIC MATERIAL | |
DE975132C (en) | Process for the production of low-fat fish meal from fatty fish | |
AT264706B (en) | Process for processing industrial hide and hide waste | |
DD223057A1 (en) | METHOD FOR THE DEPOSITION OF PROTEINS FROM PROTEIN-BASED WASTEWATERS |