![]() Device for processing viscous substances
专利摘要:
1. A DEVICE FOR TREATING VISTAIC UNITS, including 1ZICHSYA MILLS when machining., Containing a body with loading and ni irzorochnym branch pipes and the main bore, which is the main rotor, made in the form of a shaft with solid disks forming each other cameras with . with retaining zones and with outlets in the retaining zones, made in the form of overflow channels placed in the casing, the disks are mounted to form gaps with the noBepXHOCTfioio to ensure the rotation of the main rotor connected with the rotational drive, which is different in that capabilities of the device by providing processing of substances with a filler, the device is equipped with an additional rotor, made similar to the main poTopv and located parallel to it with an additional hole This is made in the housing with the possibility of intersection with the main hole to form two corner corners on the housing, separating the rotor chambers, the rotors are mounted rotatably in one direction and with the possibility of placing the disks of one rotor in the chambers of the other with the formation of clearance gaps with the shafts ensuring rotation of the rotors and the formation of retaining zones, and the bypass channels are located in at least one angular projection of the body along the tangent to the surfaces of the disks and obliquely to the longitudinal axis m rotors for communication mismat (enny7; in the direction of the longitudinal (L axes of the rotor chambers. 2. The device according to Claim 1, characterized in that in one corner protrusion there are overflow ropes for communication of the chambers of the main rotor with the additional rotor in the chamfering-1I branch pipe and in the other corner protrusion JV bypass channels are made for communication of additional rotor chambers 00 with chambers of the main rotor placed in the direction of discharge OD OO pipe 3. The device according to claim 2, characterized in that the adjacent chambers of the rotors are connected 4. The device according to claim 2, characterized in that the chambers located at least through one adjacent chamber are communicated with bypass channels. 公开号:SU1158033A3 申请号:SU833558786 申请日:1983-03-03 公开日:1985-05-23 发明作者:Нойбауер Вильхельм;Вернер Ханс 申请人:Вернер Унд Пфлейдерер (Фирма); IPC主号:
专利说明:
3 I stienio 17), so that you formulate oololimil for co-structural considerations, the clearance iiuipHnoii 1ec, how many (MHJiJJHMeTpa mecda shaft 15 (respectively 1b) listovo poR (13 (respectively 1D) and disks 17 (respectively 17) of another disk) and another disk (17) (respectively 13). Due to this kind of expansion between the two ps lying in axial direction, the disks 17 (respectively 17) of the rotor 13 (respectively 1A) are formed near the Tcj ibHo C-shaped chambers 18 (respectively 19), which are limited radially outside their wall area corresponding hole 7 (8) and inside the shaft 15 (16) and) with the outer chamber 19 of the disk 17 (respectively 17) of another rotor 14 (respectively 13) and in the axial direction upV: by the appropriate end cTopoHaNfn disks of the rotor 13 related to them (respectively 14). All bounding surfaces entering one another are, therefore, subversive. I The shafts 15 m 16 are mounted on the sub-gigs 20 in shields for p1 Picnikov 21, screwed from the outside, to the side walls 2 and 3 of the housing 1. The bearings 20 can also be placed directly in the side walls 2 and 3 of the housing 1. The passage openings 22 in the side walls 2 and 3 of the housing for the shafts 15 and 16 are equipped with the corresponding PFM 23, labyrinth seals. The drives of the burners 15 and 16 are driven from the common engine through the distribution gear (not shown). The rotors 13 and 14 are driven B in the same direction of rotation in accordance with the arrows 24 indicating the direction of rotation. Above, the rotor 13 has a charging nozzle, a funnel 25 with a BnycKHbCN bore 26 in the housing 1 and, accordingly, in the sleeve 6, which enters the first chamber 18 rotor 13. The position of this opening 26 with respect to 18 is selected so that the CTG1 inlet hole 26 is EC OTIOSIT7, the rotation of rotation is 24 24 - relative to the NPR; film 1 80334 feed rate 27, as appropriate; camera in her Ha4aJ-e. At the base of this chamber 18 — exit from it tangentially — in the lower corner projection 11, the lower bypass channel 28 is milled, which, as shown by dashed lines, is shown in FIG. 1, runs obliquely on the size (o + b): 2 in the direction of the axes 9 (respectively 10) so that it enters the displaced axis of the next camera 19 of another rotor 14. There the material is captured. Camera 19, limited to disk 17, is associated with the upper bypass 5 with a tongue 27, made on the upper corner projection 12, which (with the line of the dot-com-point is shown in FIG. 1) also with axial displacement by size (A + b): 2 leads along the tangent " 0 Whose to the disks 17 of both rotors 13, 14 and to the next chamber 18 of the rotor 13. This type of implementation is continued throughout the entire length of the housing 1, so that the material is fed through a very 5 all the time to the long path alternately through chambers 18 (respectively 19) of disk rotors 13 and 14, and this path approximately corresponds to the location of the upset Q oval. At the end of this supply path, a discharge port 30 is provided, which may be formed by a coaxial blind hole 31 in the shaft 16, which, in turn, includes a series of radial holes 32, informing the latter of the feed chamber 19 with a hole 31. Alternatively, the sleeve 30 may it is also formed by the outlet 33 in the wall 3 of the housing 1. The rotors 13 (respectively 14) can be discharged from the whole or from separate elements on shafts 15 and 16 and connected to H1rmi motionless. The housing 1 may include heating ducts 34, which, if necessary, may also be placed in the sleeve 6. 0 The sleeve 6 is usually made divided in the plane 35 of the main symmetry of the device, passing through both longitudinal axes 9 and 10 (FIG. 2), in order to be able to 5, it is possible to cut out the bypass channels 28 and 29 in a simple manner. It is also possible to perform the sleeve 6 from individual elements in the form of discs, by-pass 2-3 and 29 bypass respectively, in order to make it possible to constructively build the side walls 2 and 3 cores 1, the first in the feed direction, 7 chamber 18 of one rotor 13 and H oC {day B feed direction 27 chamber 9 of the rotor 14 of the limit; related side trunks: n -, and 2 and 3 corps 1. Vles on the pit hole 33 and 6с1 of the wall 3 of the housing 1 can also. Ш (11) can be radially exited met from the n (5, the last chamber 19, the outlet 36 in the housing 1. JUuiee, can be added in addition ;; -, -. .pments 37 l single or near d.: l) e 19 d.I am TorOf to influence, This kind of pressure ilems i7 in the simplest implementation of HiiH b1-itpl1 H1lots D B1 than the bolts of which otr: ir (5;: from the outside through the wall of Rocpus 1 into the respective chamber 9, It may be provided, except: -. | - 1, spine 38 to remove the gas, -r ;; o -); - i: -: rhVo.iRj-ibaf Mf Tep Haj. About the GKO abolishes the trail aogtsym of a viscous viscous substance and device through loads23 enters the chamber 18 of the rotor 13 "In Oi, -JTOI Hammer; 18 there is rteper-.CKHoii 28, according to which; 5th place in the displaced Chi, Kvryi -juiyw samera 19 of the other mouth P- i-;, -The content of the material is captured by both, i O1ran} 5th (t- {and this camera is 1 i / and 3 according to the current. filing 27 around the circumference at an angle equal to 270 °, jie hr. it enters the upper per1-acceleration channel 27 in the upper corner corner; - ;; 12, which also axially displaces ..- leads along a tangent to the disks 17 of both rotors 13 and 14 to the next chamber 18 of the rotor 13. This process repeats along the entire length of housing 1, so that the material is fed along a very long path alternately through the chambers 18 and 19 of the rotors 13 and 14. After finishing the MaTP.pnavn treatment, the connecting pipe 30 is exhausted. 3 Since () T, the demolition chamber 18 and 19 are separated by only movable surfaces, a high degree of self-cleaning effect is achieved. The material flows from the chamber without successful changes at the casat-1 to the rotor; uiCK: M 17 rotors, which means an obpub; -shat difficult-to-process m 1-tariffs with fillers. The embodiment of the invention in accordance with FIG. 3 apj analogous to the variant in accordance with figures 1 and 2; for this REASON -: in FIG. 3, for the same details: the same Hb v position is used; And for functionally matching parts. Drinks are the same; lochny, are positions with one or several strokes. The embodiment of the invention in compliance with 1) and Fig. 3 differs from the version in accordance with Fig. 1 in that the loading is carried out at both ends and the transfer of material does not occur in each adjacent rotor chamber located directly adjacent. The rotors 13 and 14 are provided with disks 17 in their deitral region, hence disks made on the sides, j in the form of a yonIlo cone. At one end of the housing 1 above the first chamber 18 of the rotor 13, an outlet port 26 is opened and the following inlet port 26, an inlet; it is dispersed} 1 directly next to the chamber 18 of the same rotor On the other side, the same disc rotor 13 also has an inlet opening 26g above the first chamber 18; and immediately adjacent to that of the / .e rotor 13 next to the insertion hole 26 a. From the relevant inlet -yy1-1 from 26,26 and 2 6 01 and 2 6 a to the aversti meter me 18 as in the variant in accordance with FIG. 1, the lower bypass channels 28 and 28 (respectively 27d and) lead to located directly adjacent to the feed direction of the chamber 19 of another disk rotor 14. These bypass channels 28 and 28 (respectively 28a and arranged) as in the variant in accordance with Fig. 1 and 2 in the lower, non-visible corner protrusion of the sleeve 6, in the form of a single piece. The corresponding upper overflow canapes 29 and 29 (gog) tprtgtpepei 1o and 29d) So); e pmpo ien upper yrjionoN PyS n-m tuie; 1kig-; Because they overlap the next chamber 19 of that rotor 14, they enter only the subsequent chamber 18 of the other rotor 13. Thus, from each end of the device, in an axillary direction, two streams of material-pa are supplied, largely separated from one another. , parallel to the O7cn of another to the apparatus centre in the axial direction, and this supplying process is the same as the supplying process in the device in accordance with figs 1 and 2. As follows from fig.z, both coming from each end of the supply flow enter the chamber 19 of the rotor Ii, so that respectively, in the same chamber 19, two feed streams are already combined, which are then again combined out through the discharge outlet 36. In this case, the lower overflow points 28, 28, 28c), 28c1, respectively, are shifted by size ( a + b): 2, in the longitudinal direction of the device, the upper bypass channels .24, 29, 29ci, 29d are displaced in the longitudinal direction of the device by a size of 1.5 (a + b). In the flow path, the last bypass channel is 29 and / is confused by extra size (a + b). In this embodiment, the difference between the axial distance between two adjacent pp: disks 17, 17 and the length along the axes of the disks 17, 17 is significantly increased, namely, to several millimeters, in the limiting case even to 10 mm. Due to this, between the limiting chamber 18 or 19 of the discs 17 (respectively 17), respectively, gaps 39 and TO are formed, through which the material is also pushed through, and it is subjected to a slice to a certain effect. This cpesaioiui effect can be affected if it is or the width of the gaps 39 (respectively 0) is adjustable. This can be achieved without changing the width of the gaps 39 and; iO, due to the fact that one rotor 13 Oper; lnen slightly displaced v near the longitudinal axis of the core and}. .1p -T (ro: you are connected to a pair of hydrrrrrrrrrrrrrrrrrrrrrr, rx working hours, KOTOpt. , to prevent the displacement exceeding this value, due to which the disks 17 of both rotors 13 and 14 could move axially one relative to the other, concept switches are provided. If such a displacement causes one gap 39 and one to reduce the corresponding reduction gap AO or 39, it provides more light and thus more serious: the transmission of material.From A and 5 it follows that the proposed device can also be combined with other AND details or a multi-shaft mixing and kneading device 42. At the same time, the casing 43 consisting of several sections 44, having a flange 45 at the ends, through which the individual coociio sections 44 are connected to each other. In front of the individual sections 44 of the housing, the inlet part 46 of the housing is provided with a charging nozzle 47. A motor (not shown) through the shaft 48 and the gear 49 drives d Va located parallel to each other shaft, equivalent vapam 15 c l6. Following the retraction zone 50, a beating zone 51 is located, in which the rotors 13 and 14 with the disks entering one another are located. This zone is adjacent to the zone 52 of mixing and homogenization, followed by the pressure-increasing zone 53, again equipped with the rotors 13 and 14, from which the outlet hole 54 radially extends. In this way, the supply and removal of the material to be treated in the zone 51 53, the pressure is sensed accordingly about the axial direction, from the side where, in the case of the exemplary embodiments in accordance with FIG. 13, the side walls 2 and 3 of the housing are open. As can be seen from Fig. 4, the connection of 55 with a standard pipe coupling can provide for heating the shafts 15 and 16 in the region of the pressure-boosting zone 53. as well as in the area of the zone 51 of plasticization, respectively, of the zone 52 of homogenization. As, in particular, it follows from Fig. 5, the rotors 13 and 14 in the driving area 53 are equipped with their own drive 56, For this purpose, the shafts 16 and 15 of the ET1-CX of the rotors 13 and 14 are driven to the - opposite-direction gear A9 end where they are connected with tsrivod 56. Other sections of screws 57 with i58033 I set the mppc shaft: 5 holes under the under: 59 rotors 13 and 14 on 11 ° / Ts11ig 60 60, Shafts 15 and 16 are installed with 5 bearings 61 in the section 62 section, connecting the latter to the last its enclosure section 44. Due to the correspondingly low speed drive, respectively, the rotors 13 and 14 in the pressure increase zone 53 achieve a greater pressure increase. I. 334 ™ - / I: a Xi .A: i-333: x2q 7TZHG J2 v JJ J2 J / 20 21 fpu.1 2 / " w .A - 4 t.: N Sh t -CMSSI "-SC -4-rIS - / | M : 4f t iCv4S zr ,, ,, f7 -ft.t V; 4L--. vV - r-T 15
权利要求:
Claims (4) [1] 1. DEVICE FOR PROCESSING VISCOUS SUBSTANCES, including those that become viscous during processing, comprising a housing with loading and unloading nozzles and a main hole in which the main rotor is located, made in the form of a shaft with solid disks forming chambers with retaining aeons and with exits in retaining zones, made in the form of bypass channels placed in the housing, and the disks are mounted to form from. the surface of the gaps of the day of ensuring rotation of the main rotor associated with the rotation drive, characterized in that, in order to expand the technological capabilities of the device by ensuring the processing of substances with filler, the device is equipped with an additional rotor made similar to the main ροτορν and parallel to it in the additional hole, which made in the housing with the possibility of intersection with the main hole with the formation of two angular protrusions on the housing separating the rotor chambers o, and the rotors are mounted for rotation in one direction and with the possibility of placing the disks of one rotor in the chambers of the other with the formation of gaps with shafts to ensure rotation of the rotors and the formation of retaining zones, and the bypass channels are located in at least one angular protrusion of the housing tangentially to the surfaces of the disks and inclined to the longitudinal axes of the rotors to communicate displaced in the direction of the longitudinal axes of the rotor chambers. [2] 2. The device according to claim 1, characterized in that in one corner protrusion there are bypass channels for communicating the chambers of the main rotor with cameras of the additional rotor located in the direction of the discharge pipe, and in the other corner protrusion there are bypass channels for communicating the cameras of the additional rotor the rotor with the chambers of the main rotor located in the direction of the discharge pipe " [3] 3. The device according to claim 2, characterized in that the adjacent rotor chambers are communicated by bypass channels. SP 00 about СО СО> [4] 4. The device according to claim 2, characterized in that the cameras located through at least one adjacent camera are communicated by bypass channels. fl 0 1 1-J Π ί '': Nt'DC С'ЦЦ ij'B J> O TO - pop DISCONNECTING WITH THE OPPORTUNITY '-'- Г-'ο ήηη in the direction of
类似技术:
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同族专利:
公开号 | 公开日 DE3208973C2|1984-05-30| JPS58167111A|1983-10-03| GB2116866B|1985-10-09| US4514090A|1985-04-30| IT8319970D0|1983-03-09| FR2523030B1|1988-05-27| IT1160524B|1987-03-11| DE3208973A1|1983-09-22| FR2523030A1|1983-09-16| GB8305991D0|1983-04-07| CH661682A5|1987-08-14| GB2116866A|1983-10-05|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题 DE4426441A1|1994-07-26|1996-02-01|Werner & Pfleiderer|Two-shaft screw machine, in particular two-shaft extruder| RU2505348C1|2012-07-17|2014-01-27|Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Тамбовский государственный технический университет" |Method of mixing and mixer to this end| RU2519963C1|2013-03-22|2014-06-20|Александр Федорович Короткий|Method for soaking of fibrous material with binding agent, and device for its implementation| RU2538852C2|2009-07-16|2015-01-10|Йозеф А. Блах|Extruder|GB313531A|1928-06-13|1930-05-01|Emil Faure| DE739278C|1938-07-10|1943-09-17|Ig Farbenindustrie Ag|Device for homogenizing and pressing out plastic to crumbly soft masses, emulsions and the like. like| BE473239A|1944-06-05|1900-01-01| US2670188A|1949-09-23|1954-02-23|Bayer Ag|Mixing and kneading machine| LU31896A1|1951-12-28|1900-01-01| BE516559A|1951-12-28|1900-01-01| US3042264A|1959-10-01|1962-07-03|Pyles Ind Inc|Demand mixing and dispensing machine| GB1340219A|1970-08-01|1973-12-12|Scheer & Cie C F|Devices for plasticising and extruding plastics material| US3797808A|1970-10-22|1974-03-19|Cincinnati Milacron Inc|Plastication control system for injection molding machines| DE2550969C2|1975-11-13|1982-12-16|Josef 7120 Bietigheim Blach|Screw machine for homogenizing solid, liquid and viscous materials| US4142805A|1976-02-02|1979-03-06|Usm Corporation|Method for processing polymeric material| US4194841A|1976-02-02|1980-03-25|Zehev Tadmor|Method and apparatus for processing polymeric materials| DE2648948A1|1976-10-28|1978-05-03|Gerhard Prof Dr Ing Schenkel|Drag-flow pump for rheological media - with radial or tangential feed to low and axial discharge channels from high pressure zone| DD135171A1|1978-04-10|1979-04-18|Klaus Schumann|DEVICE FOR MACHINING PLASTIC, ELASTIC OR VISCOUS MASSES| US4227816A|1978-08-21|1980-10-14|Usm Corporation|Rotary processor| US4213709A|1978-12-01|1980-07-22|Usm Corporation|Rotary processor| US4255059A|1978-12-20|1981-03-10|Usm Corporation|Processing element|DE3430885C2|1984-08-22|1986-08-21|Rudolf P. 7000 Stuttgart Fritsch|Device for the continuous processing of liquids and viscous masses| GB8605033D0|1986-02-28|1986-04-09|Shell Int Research|Fluid driven pumping apparatus| US4828036A|1987-01-05|1989-05-09|Shell Oil Company|Apparatus and method for pumping well fluids| US5137368A|1989-06-21|1992-08-11|Specified Equipment Systems Co., Inc.|Viscous fluid pumping apparatus and system| US5005982A|1989-06-21|1991-04-09|Kistner Kenneth J|Material processor| DE4013912C2|1990-04-26|1992-04-02|Fischer Karl Ind Gmbh| GB9113789D0|1991-06-26|1991-08-14|Stork Protecon Bv|Controlled shear cell and method| US5816697A|1995-12-05|1998-10-06|Teijin Limited|Viscous liquid stirring device and a process for producing polycarbonate by using the stirring device| IT1283030B1|1996-05-17|1998-04-03|Pomini Spa|PROCEDURE FOR THE CONTINUOUS MIXING OF POLYMERIC MATERIALS AND THE RELEVANT PARALLEL TANGENTIAL AND COMPENETRATING ROTOR MACHINE.| US6517232B1|1996-05-20|2003-02-11|Becker-Underwood, Inc.|Mixing systems| US7513768B2|2003-09-18|2009-04-07|United States Gypsum Company|Embedment roll device| US7182589B2|2003-09-18|2007-02-27|United States Gypsum Company|Embedment device for fiber-enhanced slurry| DE102005034456B3|2005-07-23|2006-11-02|Zimmer Ag|Device, useful for melting polycondensation of polymers under distance gaseous cleavage products in lying cylindrical reactor with agitating chamber, comprises inlet, outlet, gas channel, and outer- and inner rotor that are in chamber| DE202006008820U1|2006-06-03|2006-08-17|Frymakoruma Ag|Apparatus for dispersing and/or homogenizing liquids comprises processing unit comprising two independently rotating concentric toothed wheels driven on horizontal shafts| DE102008029130A1|2008-06-19|2009-12-24|Brückner Maschinenbau GmbH & Co. KG|Multi-screw extruder|
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申请号 | 申请日 | 专利标题 DE3208973A|DE3208973C2|1982-03-12|1982-03-12|Device for processing viscous substances or substances that become viscous during processing| 相关专利
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