GB963974A - Method and apparatus for contacting phases of different densities - Google Patents
Method and apparatus for contacting phases of different densitiesInfo
- Publication number
- GB963974A GB963974A GB3947759A GB3947759A GB963974A GB 963974 A GB963974 A GB 963974A GB 3947759 A GB3947759 A GB 3947759A GB 3947759 A GB3947759 A GB 3947759A GB 963974 A GB963974 A GB 963974A
- Authority
- GB
- United Kingdom
- Prior art keywords
- lye
- rotor
- soap
- flow
- section
- 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
- C11D13/00—Making of soap or soap solutions in general; Apparatus therefor
- C11D13/02—Boiling soap; Refining
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/04—Solvent extraction of solutions which are liquid
- B01D11/0426—Counter-current multistage extraction towers in a vertical or sloping position
- B01D11/043—Counter-current multistage extraction towers in a vertical or sloping position with stationary contacting elements, sieve plates or loose contacting elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/04—Solvent extraction of solutions which are liquid
- B01D11/0426—Counter-current multistage extraction towers in a vertical or sloping position
- B01D11/0434—Counter-current multistage extraction towers in a vertical or sloping position comprising rotating mechanisms, e.g. mixers, rotational oscillating motion, mixing pumps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/04—Solvent extraction of solutions which are liquid
- B01D11/0446—Juxtaposition of mixers-settlers
- B01D11/0457—Juxtaposition of mixers-settlers comprising rotating mechanisms, e.g. mixers, mixing pumps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/04—Solvent extraction of solutions which are liquid
- B01D11/0484—Controlling means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G21/00—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
- C10G49/10—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 with moving solid particles
- C10G49/12—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 with moving solid particles suspended in the oil, e.g. slurries
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B13/00—Recovery of fats, fatty oils or fatty acids from waste materials
- C11B13/02—Recovery of fats, fatty oils or fatty acids from waste materials from soap stock
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/74—Recovery of fats, fatty oils, fatty acids or other fatty substances, e.g. lanolin or waxes
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Detergent Compositions (AREA)
Abstract
<PICT:0963974/C1/1> <PICT:0963974/C1/2> An apparatus for mixing two liquid faces of different density and subsequently separating them comprises a container in which the flow from the rotor is arranged to change from a tangential to a radial flow. The rotor 1 is constituted by a flat circular plate 2 having eight depending vanes 3 and the diffuser 5 is constituted by an annular plate 6 having eight depending vanes 7 disposed regularly and radially of the rotor axis. The two phases flow to the centre of the rotor through an inlet pipe 8 in the direction shown by the one of the lower arrows and the outlet flow is shown by the upper arrows. Each arrangement of the rotor can constitute a stage in a multistage stage can be generally used with 10 to 16 stages.ALSO:<PICT:0963974/C4-C5/1> Crude soap is heated to 80-90 DEG C. and pumped by means of pump 40 to the washing unit at a predetermined rate in an even flow. The anhydrous soap content of the crude soap should not exceed 57%; it may be adjusted by mixing in a small amount of spent lye from pipe 41. The brine, of a constant predetermined composition, after heating to about 90 DEG C. is fed through inlet pipe 42. The flow of the brine is controlled by a valve 43 responsive to the interfacial float 44. The mixture of crude soap and lye enters the unit through the inlet distributer 45. The soap separates from the lye and floats upwards under the conical baffles 28, 29, until it reaches the rotor 1. The lye settles to the bottom and is partly pumped round the circulation system again, partly taken out of the system as spent lye through pipe 41. The rotor 1, being a pump wheel, circulates the lye in the lowest section continuously, the lye flowing to it through the narrow space between the conical baffles. The soap from the bottom of the tank and the lye in the bottom section mix in the rotor of that section and the resulting intimate mixture of lye and soap is thrown out of the rotor against the diffuser and flows then radially in a quiet fashion, into the settling space of the bottom section. The soap floats upwards and passes into the rotor of the next upper section. The lye flows downwards and then upwards between the conical baffles, partly into the rotor of the bottom section again, where it is mixed with fresh soap, and partly into the bottom of the tank, to replace the outgoing glycerine lye, which is withdrawn from the lye circulation system. All the intermediate sections of the washing unit are alike. The soap is settled in the top section. The settled soap 48 runs off over a weir 46 and pipe 47. The sodium chloride may be wholly or partially replaced by other salting out electrolytes such as sodium hydroxide and the temperature should not be allowed to drop below 85 DEG C. A modified arrangement for the neutralizing of a glycerine lye containing up to 2% of a free alkali with fat containing up to 20% of free acids is described in Fig. 13 (not shown).
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3947759A GB963974A (en) | 1959-11-20 | 1959-11-20 | Method and apparatus for contacting phases of different densities |
SE1110260A SE301302B (en) | 1959-11-20 | 1960-11-18 | |
ES0262607A ES262607A1 (en) | 1959-11-20 | 1960-11-19 | Method and apparatus for contacting phases of different densities |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3947759A GB963974A (en) | 1959-11-20 | 1959-11-20 | Method and apparatus for contacting phases of different densities |
Publications (1)
Publication Number | Publication Date |
---|---|
GB963974A true GB963974A (en) | 1964-07-15 |
Family
ID=10409761
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3947759A Expired GB963974A (en) | 1959-11-20 | 1959-11-20 | Method and apparatus for contacting phases of different densities |
Country Status (3)
Country | Link |
---|---|
ES (1) | ES262607A1 (en) |
GB (1) | GB963974A (en) |
SE (1) | SE301302B (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111494985A (en) * | 2020-05-25 | 2020-08-07 | 张掖征峰科技有限公司 | Multistage continuous countercurrent washing leaching equipment and method |
-
1959
- 1959-11-20 GB GB3947759A patent/GB963974A/en not_active Expired
-
1960
- 1960-11-18 SE SE1110260A patent/SE301302B/xx unknown
- 1960-11-19 ES ES0262607A patent/ES262607A1/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111494985A (en) * | 2020-05-25 | 2020-08-07 | 张掖征峰科技有限公司 | Multistage continuous countercurrent washing leaching equipment and method |
Also Published As
Publication number | Publication date |
---|---|
ES262607A1 (en) | 1961-04-01 |
SE301302B (en) | 1968-06-04 |
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