• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The invention relates to a process for the extraction of solids from liquids containing solids granulated by heat effect and/or solids the moisture content of which is reducible by heat effect, especially from colloidal solutions with protein content, suspensions and slurries for reducing the fat content of the solid material, in the course of this process grains are formed in the liquid with heat effect, or the moisture content of the grains is reduced, then they are removed from the liquids and dried. The equipment for implementation of the process is also subject of the invention. The process is characterized by heating the liquid to 50 DEG -125 DEG C. temperature with heat transfer ("instant heating") for a short period, maximum for 2 minutes, then the heated material is kept at 50 DEG -125 DEG C. temperature for at least 2, preferably for 5-15 minutes. This is followed by separation of the grains from the liquid phase with filtration in a space containing vapor of 50 DEG -125 DEG C. temperature, the filtration process carried out in minimum 4, preferably in 8-15 minutes. Should the solid material contain fat, then at least a certain part of the fat is melted with the heat treatment processes. Finally the wet solid material separated from the liquid is dried. The equipment is provided with collection tank, instant heater, preferably with gravitational filter arranged in closed space, as well as with a drier. These are united in a closed system with pipelines and feeder device(s), with one or several pumps incorporated in the system. Advantage of the invention is that the extraction of the solid content of solutions, slurries etc., which are difficult to treat and reduction of the possible fat content of the solid material are realized with a simple means in such a way, that an excellent end-product is available in respect of both the qualitative and other utilization properties.
    公开号:SU955846A3
    申请号:SU802897653
    申请日:1980-03-20
    公开日:1982-08-30
    发明作者:Такач Иштван；Керей Дьердь；Рудольф Петер；Иллеш Янош；Сабо Бела；Верецкеи Эндре；Банаш Золтан；Бошитш Дьюла；Чебе Ласло
    申请人:Рихтер Гедеон Ведьесети Дьяр Рт (Инопредприятие)；
    IPC主号:
    专利说明:

    At the same time, during filtration, the wastewater is washed with water at the TZ-EO C. This goal is also achieved by the fact that the installation for separating protein from wastewater containing giro-protein impurities, including the collecting tank, filter and dryer, is fitted in series between the collecting tank and filter device for pre-heating and a device for heat treatment of water, as well as a screw auger and a metering device located between the filter and the dryer. At the same time, the collection tank is equipped with a stirrer and p circulating tube conductor with a pump. In addition, the collecting tank and the pre-heating device are interconnected by a pipe with a pump mounted therein, and a tank for washing water and a device for metering the substance used for protein precipitation are located between the latter and the collection tank. At the same time, the preheating device consists of vertically placed pipes one inside the other, the inner of which is perforated and has a curved solid end, and the outer one is made with an extension in the upper part. The filter consists of two parts, one of which is made in the form of a truncated cone, installed with the possibility of rotation, and the friend consists of a polygon-shaped cross-sectional link, and their longitudinal axes form a zigzag line. parts made a hole, eccentric located relative to the axis of rotation. Nin cone. In this case, the dryer is a horizontally disposed cylinder, inside which there are discs alternating with each other, some of which are equipped with scrapers and others are rollers, with disks with scrapers having holes in the hanging and disks with rollers - holes along the periphery. In addition, the installation of hay hay by a device for absorbing odors connected to the filter and washing. device associated with a dryer. FIG. 1 is a schematic representation of the installation. For the isolation of protein from the wastewater of the mill at FIG. 2 - a device for preliminary heating and heat treatment of water. The installation includes a collection tank 1 with a supply pipe 2 and a recirculation pipe 3 with a pump 4 and a stirrer 5, a filter, a dryer sequentially installed between the collection tank 1 and a filter, a preheating device and a heat treatment device 6 between the filter and and the dryer screw screw 7 and the metering device 8. The collection tank 1 and the device for preheating the water are interconnected by a pipe 9 with a pump 10 mounted inside it, and between the pump 10 and the assembly second capacitance; there is a washing water tank 11 and a device 12 for dispensing a substance used for the precipitation of proteins. The device for preheating water consists of inner and outer tubes 13 and 14 arranged one inside the other, the inner tube 12 being perforated with holes 15, and the outer tube 14 is made with expansion 16 in the upper part. The filter consists of two parts, one of which is made in the form of a truncated cone 17 rotatably mounted, and the other consists of links 18-20 interconnected which have a polygon shape in cross section, and their longitudinal axes form a zigzag line. At the junction of the filter parts, a hole 21 is made, eccentrically located relative to the axis of rotation of the cone 17. The side surfaces of the cone 17 and links 18-20 are partially formed by the filtering surface 22. The lower part of the cone is designed as a bath 23 with a nozzle 24 for removing the filtrate. A flushing device consisting of a pipe 25 with spray heads 26 arranged on it is mounted in the upper part of the filter for flushing the outer surface of the hollow element 27, using water, steam, high pressure water or compressed air as the washing liquid . The installation is equipped with an odor absorption device 28 connected to a filter, which can be used as a scrubber, absorber, or the like. The dryer is a horizontal cylinder 29, inside which there are alternating discs 30 with scrapers 31 and discs 32 with rollers 33, while the discs 30 have holes 34 in the shaft (not shown), and discs 32 from the periphery 35 . amount
    There can be up to four scrapers or rollers on each disc, while they are located on the discs at an angle of 90 V. A dust collector with a dust bag (not shown), connected by a duct 36 with an absorption device 28, is fixed to the dryer. odors. On both sides of the dryer there are nozzles 37 and 38 for the supply of dry gas. For unloading the product there is a pipe 39 in which a paddle feeder 40 is fixed.
    The devices for heat treatment and for preheating of water are connected by a pipe 41 connected to the control unit 42, and a device for the heat treatment of water by means of a pipe 43 is connected to a filter.
    The method is carried out as follows.
    An aqueous suspension of wastewater, mainly wastewater of socombinate containing giroprobny impurities with a solids content of about 2-5% is sent to the collection tank 1 and using a pump 4 and / or mixer 5 is subjected to homogenization to prevent coagulation values of associated substances, which are then easily removed by filtration by washing and removal with a filtrate. Then, the material is pumped by pump 10 into a pre-heating device, in which steam passes through a perforated pipe 13 for 2 minutes into the material under a pressure of 0.2-0.4 bar at 50-125 ° C. l (proteins) lose their hydrophilic-colloidal properties. If the fluid contains pharmacologically valuable substances, such as heparin, it is released completely in bound form with the coagulable proteins and then separated by filtration.
    Further, the material is fed to a heat treatment device b, where it is treated at 50-125 ° C for 7-15 minutes, while the released flakes of particles increase, they are hydrophilic and therefore partially lose the ability to coagulate, but become harder and as a result, they can be easily separated in the future.
    Many bacteria are destroyed in the heating process, and dehydration occurs in the stuck particles
    Then the material is fed through the pipeline 43 into the filter, while the filtration is carried out at 5 O-12B C in the steam-saturated chamber 44 for 8-. 15 minutes. In the cone 17, the material is pre-dehydrated. In links x 1820 filter the wet mass of the material is subjected to transverse return-pos-t
    dull motion and slow forward motion, whereby the mass is divided into separate parts, while the filter surface 22 is continuously cleaned and replaced with a new one. In the hollow element 27, the material is divided into two fractions: the filtrate and the filtered residue with a content of 15-35% solids. Together with the filtrate collected
    0 in the bath 23 and removed through the pipe 24, non aggregated and associated ballast materials are removed, for example, most of the melted fat.
    5 Valuable constituents of the starting material, approximately 97-99%, are bound to the coagulating protein. The associated substance (fat) is in the filter in the liquid state and during oscillatory movement of the mass of the material is removed mostly in the hollow element 27. Removable through the tube 45 of the screw auger 7, the particles of the processed material have quite
    5 large sizes.
    The fat from the filtrate exiting through the nozzle 24 is separated by a separator (not shown) or by cooling. The defatted filtrate as a washing liquid can be recycled back to or into the hollow element 27. The steam rising in the chamber 44 is condensed and removed along with the filtrate. The non-condensable portion of conduit 46 is directed to odor absorption unit 28. A washer is used for continuous injection through spray heads 26 during
    0 the process of filtering chemicals for chemical treatment of a material or for supplying hot water during degreasing.
    Then the filtered material
    5 is subjected to contact and heat treatment in a dryer, where due to separation of the latter by disks 30 and 32, the residence time of the material increases, since the particles of the material
    0 move on the way from the wall of cylinder 29 and then back. Through pipes 37 and 38 dry air is supplied to the interior of the dryer, and drying is carried out with a gas stream with a temperature of 100-180 ° C.
    5 for 20-40 minutes, whereby the rollers 33 scrape the material to the inner wall and the dried material is removed by scrapers 31 and distributed in the air flow. The rollers 33 also serve to grind the material separated from the wall to particles of a given size, while the particle size is controlled by setting a predetermined distance of the rollers from the wall of the cylinder 29. The exhaust air is cleaned in a dust collector (not shown) and
    . in device 28 for absorbing odors.
    The finished product leaves the dryer through a paddle dispenser, has 90% solids with a uniform particle size, the number of microorganisms is only germ / g and then using air filters (not shown), this quantity of germ is adjusted to several spores per gram,
    Example 1. In a milling enterprise with wet spitting pork fat using steam at 92–9 & In the decanter, the material containing protein, a large amount of fat and water is separated, and the fat is 25-50% of the total solids content and water is 6070% of the total weight.
    Water with a temperature of 82 ° C is added to this material and the diluted material is pumped to the collection. The solids content in the material is controlled within 5-15%. By means of a slurry or suspension pump, the fluid is circulated continuously to homogenize it and increase the surface of the bulk material and, therefore, better defatting.
    The homogenized liquid is fed by a dosing pump into a preheating device, in which steam is supplied to a temperature of 92–96 ° C by supplying steam for 30 s under a pressure of 0.5 atm.
    During the heat treatment, the bulk of the fat is melted and mixed with boiling water, while the particles, after the heat treatment, continue to coagulate and aggregate and acquire the ability to separate on the filter.
    The coupled particles are continuously separated into water-containing grease on a gravity filter in a vapor atmosphere at 90, c. During filtration, water is rinsed at 82 ° C from the top through the spray heads of the washer.
    The fat-containing filtrate is treated further in a known manner, and the protein-containing material freed from most of its fat is subjected to continuous air drying at 140-150 ° C for 35 minutes in a dryer. The quality of the material at this temperature does not deteriorate - The finished product has the following components,%: moisture-7.8, protein 79.7, digestible protein 97.4 (total protein content), fat 11.8. the number of embryos in gram 1500.
    The finished product is well preserved, can be cheaply transported, has low embryo content and is low in fat, the content of digestible protein is high. Ready. The product is suitable for use as animal feed.
    Example 2. The cattle's rectal intestines, collected at the m processing enterprise, are crushed on an industrial top with; diameter of holes 6-8 mm. The crushed feedstock contains approximately 17% of dry substances and is washed into the tank with water of 15-25 C. To this raw material is added
    5 water until the solids content of the suspension is 4-7% and is subjected to prolonged recirculation using a slurry pump for homogenization. Homogenized material fall to the device
    0 for preheating, in which steam is heated at 0.5 atm. before. 87-93 ° C, and sent to a heat treatment apparatus, where it is kept at the same temperature.
    e 12 Min, while the particles lose their hydrophilic character and become insoluble in water, lose some of the structural water and agglomerate before forming well-filtered elastic particles. The main part of the fat melts and forms an aqueous emulsion with water, the microorganisms are largely destroyed. The coagulant containing most of the proteins is separated in the steam chamber by filtration at 90 ° C from the fat containing protein hydrolysates (perlides, peptides) in insignificant amounts. During filtration from the top, water is rinsed at 80 ° C to remove residual fat.
    The filtered material is dried in example 1.
    The final product has the following components,%: moisture 9.2, fat 9.7,
    5 protein 72.4; digestible protein
    (total protein) 96.2, Number of germs per 1 g 3500. I
    The final product has a high storage capacity, high quality, contains a small amount of microorganisms, a small amount of fat and a large amount of digestible protein. The product can be effectively used as
    5 animal feed. Due to
    repeated heat treatment and filtration process precludes prior removal of experiments from the rectum.
    0 — Example 3. The blood of animals continuously collected on the m processing plant is subjected to clotting, for example with the help of kala chloride (and, and carefully ground
    权利要求:
    Claims (9)
    [1]
    5 into pieces of 10-15 mm in size, then mixed with water at and the resulting mass or suspension is reheated in a device for preheating with live steam at 0, 5 atm L to 95-100 C. Then the material is kept at the same temperature for 8 minutes in the device for thermal treatment, while the protein of coagulated blood due to the effect of heat loses its hydrophilicity during the heat treatment, forming elastic particles that can be well filtered. The coagulum separated during filtration contains 25% dry matter (the initial dry matter content in the blood is 19%). The chemical used to accelerate blood coagulation is removed along with the filtrate, the filtered matter is dried at 120-180 ° C at the inlet and at 80-85 ° C at the outlet for 25 minutes. The final product contains the following components,%: dry Chemicals 90, - water 8.7; fat 0.4, protein 89.2, digestible protein (total protein) 98.0. The number of germs per 1 g is 4800. The granulate obtained is durable, has a high storage capacity and can be used as animal feed. The proposed method provides high-quality products with a moisture content of 5-15%. The unit used to carry out the process forms a closed system, the cleaning of the material is carried out under the conditions of absence of decomposition and the formation of odors. The reproduction of microorganisms and enzyme activity at the very beginning of the process is inhibited by rapid growth. In a closed installation system, the enzyme degeneracy is slowed down during the whole process, the degreasing process is carried out automatically and the final product is released in the form of amorphous grains with high specific surface, constant composition and capable of long-term storage. The devices used are simple in their design, to manage the installation, a small number of service personnel is required, the capital costs for the installation are low, and also non-wasteful energy consumption. Claim 1, a method for separating protein from wastewater containing fat-protein admixtures, which include treating water with a substance to precipitate proteins, heating, separating sludge and drying, characterized in that, in order to intensify the process, the heating is carried out in two stages, the first of which is carried out for 12 minutes at 50-125 ° C, and the second 7-15 minutes at 50-125 ° C, and the precipitate is separated by filtration in a steam-saturated chamber at the same temperature for 8-15 minutes.
    2. The method according to p. 1, characterized in that the drying is carried out with a gas stream with a temperature of 100180 C for 20-40 minutes {
    [2]
    3. The method according to claim 1, characterized in that the waste water is subjected to homogenization before heating. . .
    [3]
    4. A method according to claim 1, characterized in that the heating during the first two minutes is conducted with live steam under a pressure of 0.2-0.6 at.
    [4]
    5. The method of PoP | 1, which differs from the fact that during filtration, the wastewater is washed with water at 75-90 C.
    [5]
    6. An installation for carrying out the method according to claim 1, including an assembly tank, a filter and a dryer, so that, in order to increase the productivity, it is supplied in series with the installed modular tank and a filter with a preheating device and a device for heat treatment of water, as well as a screw auger and a metering device located between the filter and the dryer,
    [6]
    7. Installation according to Claim 6, characterized in that the collecting vessel is provided with a bag and a recirculation pipe with a pump.
    [7]
    8. Installation according to claim 6, distinguished from; by the fact that the collecting tank and the preheating device are interconnected by a pipeline with a pump mounted therein, and between the latter and the collecting tank there is a container for ALARM water and a device for metering the substance used for protein precipitation.
    [8]
    9. The installation according to claim b, characterized in that the preheating device consists of pipes vertically arranged one inside the other, the inside of which is perforated and has a CURVE solid end, and the outside is made with an extension in the upper part. Installation according to claim 6, which is distinguished by the fact that the filter consists of two parts, one of which is made in the form of a truncated cone mounted for rotation, and the other consists of interconnected links having the shape of a polygon in cross section ka, and their longitudinal axes form a zigzag line, wherein at the connection portions is a hole, located eccentrically relative to the axis of rotation of the cone.
    [9]
    11. Installation according to claim 6, characterized in that the dryer is a horizontal cylinder, inside which there are alternating disks, one of which is equipped with scrapers and others with rollers, and the disks with scrapers have an opening at the shaft, and discs with rollers holes on the periphery.
    12. Installation according to claim 6, which is equipped with a device for absorbing odors, connected to the filter and the washing device associated with the dryer.
    Sources of information, П1Л Н тые into consideration during examination
    1. Overview information. Seri M sleep industry. The use of fidiko-chemical methods in the preliminary treatment of wastewater and mocombinates. M., 1977, No. 23, p. 26.
    2. Express information. M sleep industry, M., 19.75, No. 6, p. 15-14.
    17 f l l and / 7 W, f. L
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    同族专利:
    公开号 | 公开日
    DK154005B|1988-10-03|
    JPS6243651B2|1987-09-16|
    US4539111A|1985-09-03|
    FR2451767B1|1984-04-27|
    ES490539A0|1981-03-16|
    ZA801562B|1981-06-24|
    DK154005C|1989-02-13|
    IN152917B|1984-05-05|
    AR225435A1|1982-03-31|
    HU184673B|1984-09-28|
    YU42080B|1988-04-30|
    DE3011025A1|1980-10-02|
    US4406795A|1983-09-27|
    IT1133069B|1986-07-09|
    PL126546B1|1983-08-31|
    SE466934B|1992-05-04|
    NL8001691A|1980-09-23|
    YU42970B|1989-02-28|
    AT386400B|1988-08-10|
    SE8002123L|1980-09-22|
    GB2049648B|1983-08-03|
    DE3011025C2|1989-07-20|
    DK119580A|1980-09-22|
    BR8001719A|1980-11-18|
    BE882372A|1980-09-22|
    ES8103552A1|1981-03-16|
    NL184156C|1989-05-01|
    AU5663480A|1980-09-25|
    YU78880A|1983-12-31|
    YU161183A|1984-02-29|
    IT8067439D0|1980-03-21|
    GR67678B|1981-09-04|
    NZ193189A|1984-10-19|
    CS248009B2|1987-01-15|
    PL222909A1|1981-02-13|
    AU536969B2|1984-05-31|
    ATA141780A|1988-01-15|
    FR2451767A1|1980-10-17|
    DD149469A5|1981-07-15|
    CA1141943A|1983-03-01|
    GB2049648A|1980-12-31|
    JPS55162945A|1980-12-18|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    RU2454371C1|2010-11-02|2012-06-27|Федеральное государственное образовательное учреждение высшего профессионального образования "Мурманский государственный технический университет" |Method of effluents treatment|US3057076A|1958-05-26|1962-10-09|Ind Powertronix Inc|Recovery system|
    US3046286A|1959-02-06|1962-07-24|Armour & Co|Process for recovering fats and meat and bone scrap from inedible slaughterhouse materials|
    GB962076A|1961-06-09|1964-06-24|Mueller Hans|Filtering process|
    US3348599A|1964-04-03|1967-10-24|Scientism Lab|Apparatus for dewatering and dehydrating slimes and the like|
    DE1608356A1|1967-12-01|1970-12-10|Metallgesellschaft Ag|Process for dewatering slurries by heating and adding flocculants|
    FR2107581A5|1970-09-16|1972-05-05|Pont Brule|Purifying water contng proteins and opt lip- - ids |
    US3744543A|1970-10-30|1973-07-10|Envirotech Corp|Method for steam drying filter cake|
    US3697417A|1971-03-02|1972-10-10|Sterling Drug Inc|Heat treatment of sewage sludge|
    DE2311568A1|1972-03-20|1973-09-27|Alwatech As|PROCEDURE FOR THICKENING AN AQUATIC PROTEIN-CONTAINING SLUDGE|
    US3936375A|1972-03-20|1976-02-03|A/S Apothekernes Laboratorium For Specialpraeparater|Process for dewatering a proteinaceous, aqueous sludge and for removing and recovering precipitating agents from a precipitate containing proteinaceous substances|
    US3959125A|1974-07-05|1976-05-25|Sterling Drug Inc.|Treatment and disposal of sewage sludge|
    NO140878C|1975-08-21|1979-12-05|Myrens Verksted As|PROCEDURE FOR FILTERING FINE GRAIN SOLID PRODUCTS FROM A LIQUID SUSPENSION AND DRYING OF THE FILTERED PRODUCTS, AND FACILITIES FOR USE WHEN PERFORMING THE PROCEDURE|
    US4133756A|1976-02-20|1979-01-09|Sumitomo Heavy Industries, Ltd.|Method for dehydrating a mixed dust slurry|
    SE421990B|1977-01-27|1982-02-15|Alfa Laval Ab|PROCEDURE FOR DIVISION OF ANIMAL ORIGINAL PRODUCTS INTO A FAT FRACTION AND ATMINSTONE A PROTEIN FRACTION|
    HU184670B|1979-03-21|1984-09-28|Richter Gedeon Vegyeszet|Apparatus for filtering sludge, suspension or similar material, or cleaning by washing and/or separating from fluid lumpy solid material, or sizing solid granular materials|US4615801A|1984-10-29|1986-10-07|Lee Chung Y|Rotary filtration means in the filth condensation-dehydration apparatus|
    US4728517A|1984-12-03|1988-03-01|Markham William M|Conversion of biological sludge and primary float sludge to animal protein supplement|
    FR2597362B1|1986-04-22|1991-07-26|Guinard Oil Services|METHOD AND INSTALLATION FOR SEPARATING THE CONSTITUENTS OF A SUSPENSION.|
    US4844799A|1986-07-17|1989-07-04|Lee Chung Y|Filtration apparatus having spaced-apart driving members for changing a size of a treatment zone|
    JPH0510931Y2|1987-12-21|1993-03-17|
    DE3821242A1|1988-06-23|1989-12-28|Antonio M Dipl Ing Celi|METHOD AND DEVICE FOR PROCESSING METAL-LOADED WASTE SLUDGE|
    WO1992019547A1|1991-05-01|1992-11-12|Level Valley Dairy Company|Wastewater treatment system|
    DE4402311C2|1993-02-06|1998-02-26|Kronos Titan Gmbh|Process for improving the filtration of sulfur-containing suspensions|
    DE4427432A1|1994-08-03|1996-02-08|Hubert Wilz|Method and arrangement for the continuous removal of filterable substances from a liquid|
    US6159360A|1996-11-22|2000-12-12|Heinkel Industriezentrifugen Gmbh & Co.|Invertible filter centrifuge including a solids drier|
    DE19832916A1|1998-07-22|2000-02-03|Michael Betz|Method and device for separating process and / or waste water with a predetermined concentration of coagulable, hydrophobic constituents into a hydrophobic phase and a clear phase|
    DE19902644A1|1999-01-23|2000-08-03|Hdl Naturprodukte Gmbh|Evaporation plant treating effluent from hide and skin preservation process, operates two stage heating process, to flocculate and filter out contaminants, recovering salt for recycle to process|
    WO2001037677A1|1999-11-23|2001-05-31|Novus International, Inc.|Process for isolating and preparing a dry proteinaceous material from waste water|
    EP1420653A4|2001-08-03|2005-09-21|Mars Inc|Method of utilising offals for pet food manufacture|
    US6905609B2|2003-02-06|2005-06-14|Namon A. Nassef|Waste treatment and disposal system|
    NO320978B1|2005-01-13|2006-02-20|Asbjorn Hammer|Device for drying material|
    JP5552668B2|2010-03-30|2014-07-16|静岡県|Method and apparatus for recovering water-soluble protein|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    HU79RI703A|HU184673B|1979-03-21|1979-03-21|Method and apparatus for yielding the solid material from fluids e.g. colloidlike solutions, sludges and suspensions containing protein and grease the solid content of which may be granulated by heat effect and/or the moisture content of solid content of which may be decreased by heat effect|
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