CN109487608B - Continuous double-vortex hydraulic cleaner - Google Patents

Continuous double-vortex hydraulic cleaner Download PDF

Info

Publication number
CN109487608B
CN109487608B CN201811544824.XA CN201811544824A CN109487608B CN 109487608 B CN109487608 B CN 109487608B CN 201811544824 A CN201811544824 A CN 201811544824A CN 109487608 B CN109487608 B CN 109487608B
Authority
CN
China
Prior art keywords
slurry
cavity
slurry cavity
impeller
vortex
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.)
Active
Application number
CN201811544824.XA
Other languages
Chinese (zh)
Other versions
CN109487608A (en
Inventor
庞同国
李克雷
岳林
崔利胜
王泽刚
荆强
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shandong Chenzhong Machinery Co ltd
Original Assignee
Shandong Chenzhong Machinery Co ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shandong Chenzhong Machinery Co ltd filed Critical Shandong Chenzhong Machinery Co ltd
Priority to CN201811544824.XA priority Critical patent/CN109487608B/en
Publication of CN109487608A publication Critical patent/CN109487608A/en
Application granted granted Critical
Publication of CN109487608B publication Critical patent/CN109487608B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21BFIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00Fibrous raw materials or their mechanical treatment
    • D21B1/04Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
    • D21B1/12Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
    • D21B1/30Defibrating by other means
    • D21B1/34Kneading or mixing; Pulpers
    • D21B1/345Pulpers

Landscapes

  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Mechanical Engineering (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

The invention discloses a continuous double-vortex hydraulic cleaner, wherein a slurry tank comprises a cylindrical first slurry cavity and a cylindrical second slurry cavity, and the lower end of the first slurry cavity is communicated with the upper end of the second slurry cavity; the first slurry cavity is obliquely arranged relative to the ground, and the impeller is arranged at the upper end of the first slurry cavity; the caliber of the second slurry cavity is gradually reduced along the direction from the upper end to the lower end. Through carrying out structural improvement on the slurry tank, the first slurry cavity is obliquely arranged, the caliber of the second slurry cavity is gradually reduced, the purpose that the slurry forms vortex in the first slurry cavity and the second slurry cavity at the same time can be achieved, the vortex flow direction in the first slurry cavity is opposite to the vortex flow direction in the second slurry cavity, the slurry flow circulation effect is improved, and the slurry mixing speed is accelerated; the bidirectional double vortex flow can effectively reduce the flow resistance of the slurry flow thrown out by the impeller after rising along the groove wall, improve the slurry flow state, reduce the energy loss and improve the production efficiency.

Description

一种连续式双涡流水力清洗机A continuous double vortex hydraulic cleaning machine

技术领域Technical Field

本发明涉及造纸制桨领域,更具体的说是涉及一种连续式双涡流水力清洗机。The invention relates to the field of papermaking and paddle making, and more particularly to a continuous double-vortex hydraulic cleaning machine.

背景技术Background technique

水力清洗机用于造纸制浆行业废纸处理流程中除去纸浆中的大量轻质及少量重质杂物,工作时,随着转子的旋转,投入清洗机的浆料受到水力冲击、叶轮的机械撕扯及叶轮与筛板间的机械疏解,产生强力的剪切、摩擦和揉搓作用,使清洗机内的浆料得到充分碎解,最后被离解成纤维。Hydraulic cleaning machine is used to remove a large amount of light and a small amount of heavy debris from the pulp in the waste paper processing process of the papermaking and pulping industry. During operation, as the rotor rotates, the pulp put into the cleaning machine is subjected to hydraulic impact, mechanical tearing of the impeller, and mechanical disintegration between the impeller and the screen plate, generating strong shearing, friction and kneading effects, so that the pulp in the cleaning machine is fully broken down and finally dissociated into fibers.

现有水力清洗机如图1所示,设备整体布局为水平式结构,第一,浆料在卧式浆槽1内不能形成涡流,无法实现浆料的强力冲撞和打散,不利于浆料的碎解;第二,浆槽1的良浆出口3和重渣出口5均在浆槽下部,良浆和杂质分离不彻底。该结构也决定了良浆和杂质的排放为间歇式,大大降低了生产能力和效率;第三,如图1所示,叶轮2的轮芯较大,叶片较高较短,增加了流动阻力,进而增加了设备能耗。The existing hydraulic cleaning machine is shown in Figure 1. The overall layout of the equipment is a horizontal structure. First, the slurry cannot form a vortex in the horizontal slurry tank 1, and the slurry cannot be strongly impacted and broken up, which is not conducive to the crushing of the slurry; second, the good slurry outlet 3 and the heavy slag outlet 5 of the slurry tank 1 are both at the bottom of the slurry tank, and the good slurry and impurities are not completely separated. This structure also determines that the discharge of good slurry and impurities is intermittent, which greatly reduces the production capacity and efficiency; third, as shown in Figure 1, the impeller 2 has a larger wheel core and higher and shorter blades, which increases the flow resistance and thus increases the energy consumption of the equipment.

因此,如何提供一种能够解决上述全部或部分缺陷的清洗机成为本领域人员亟需解决的一个技术问题。Therefore, how to provide a cleaning machine that can solve all or part of the above-mentioned defects has become a technical problem that people in this field need to solve urgently.

发明内容Summary of the invention

有鉴于此,本发明提供了一种连续式双涡流水力清洗机,所述清洗机具有浆槽,所述浆槽上开设有进桨口、重渣出口和良桨出口,所述浆槽内设置有叶轮;In view of this, the present invention provides a continuous double-vortex hydraulic cleaning machine, the cleaning machine has a pulp tank, the pulp tank is provided with a pulp inlet, a heavy residue outlet and a good pulp outlet, and an impeller is arranged in the pulp tank;

所述浆槽内具有筒形的第一浆料腔和第二浆料腔,所述第一浆料腔的下端与所述第二浆料腔的上端连通;所述第一浆料腔相对于地面倾斜设置,所述叶轮安装于所述第一浆料腔的侧壁上端;所述第二浆料腔的横截面沿其上端至下端的方向逐渐变小。The slurry trough comprises a first cylindrical slurry chamber and a second cylindrical slurry chamber, wherein the lower end of the first slurry chamber is connected with the upper end of the second slurry chamber; the first slurry chamber is inclined relative to the ground, and the impeller is installed at the upper end of the side wall of the first slurry chamber; the cross-section of the second slurry chamber gradually decreases from its upper end to its lower end.

本发明的有益效果是:通过对浆槽进行结构改进,使第一浆料腔倾斜设置,第二浆料腔口径逐渐减小,能够实现浆料同时在第一浆料腔及第二浆料腔内形成涡流,且第一浆料腔内的涡流与第二浆料腔内的涡流流向相反,改善了浆流循环效果,加速了浆液混合速度;双向双涡流能有效减轻叶轮抛出的浆流沿槽壁上升后返转的流动阻力,改善浆料流态,减少能量损耗。The beneficial effects of the present invention are as follows: by improving the structure of the slurry trough, the first slurry chamber is tilted and the diameter of the second slurry chamber is gradually reduced, so that the slurry can form vortices in the first slurry chamber and the second slurry chamber at the same time, and the vortex in the first slurry chamber and the vortex in the second slurry chamber flow in opposite directions, thereby improving the slurry flow circulation effect and accelerating the slurry mixing speed; the bidirectional double vortex can effectively reduce the flow resistance of the slurry flow thrown out by the impeller and then returning after rising along the trough wall, thereby improving the slurry flow state and reducing energy loss.

优选的,第一浆料腔的中心轴线相对于地面的倾斜角度为45°-55°,倾斜角度可根据浆料内的重渣多少进行适当调整,当重渣较多时可增大角度提高重渣的收集效果。Preferably, the inclination angle of the central axis of the first slurry chamber relative to the ground is 45°-55°, and the inclination angle can be appropriately adjusted according to the amount of heavy slag in the slurry. When there is a lot of heavy slag, the angle can be increased to improve the collection effect of the heavy slag.

优选的,所述进桨口设置于所述第一浆料腔靠近下端的侧壁上,所述良桨出口设置于所述第一浆料腔靠近上端的侧壁上,所述重渣出口设置于第二浆料腔的下端。Preferably, the paddle inlet is arranged on the side wall of the first slurry chamber near the lower end, the good paddle outlet is arranged on the side wall of the first slurry chamber near the upper end, and the heavy slag outlet is arranged at the lower end of the second slurry chamber.

良浆出口和重渣出口分别设计在第一浆料腔靠近上端的侧壁上以及第二浆料腔的下端,运行时能够实现良浆和重渣的彻底分离,实现了连续出桨;与现有水力清洗机相比,节能效率可达25%左右,对相同规格的水力清洗机来说,在同等的碎解度下,可提升产能10-30%。The good pulp outlet and the heavy slag outlet are designed on the side wall near the upper end of the first slurry chamber and the lower end of the second slurry chamber respectively. During operation, the good pulp and heavy slag can be completely separated, and continuous slurry discharge is realized. Compared with the existing hydraulic cleaning machine, the energy saving efficiency can reach about 25%. For hydraulic cleaning machines of the same specifications, at the same crushing degree, the production capacity can be increased by 10-30%.

进一步的,还包括支撑座,所述支撑座一端设置于地面上,另一端与所述第一浆料腔和/或第二浆料腔的外侧壁连接。Furthermore, it also includes a support seat, one end of which is set on the ground, and the other end is connected to the outer side wall of the first slurry chamber and/or the second slurry chamber.

通过支撑座可对清洗机整体进行辅助固定,防止清洗机由于浆槽倾斜产生装置侧翻的问题。The support seat can be used to assist in fixing the entire cleaning machine to prevent the cleaning machine from tipping over due to the tilt of the pulp tank.

进一步的,还包括驱动电机和外壳,所述驱动电机的驱动轴与所述叶轮传动连接,所述外壳覆盖设置于所述驱动电机上。Furthermore, it also includes a driving motor and a casing, wherein the driving shaft of the driving motor is drivingly connected to the impeller, and the casing is covered on the driving motor.

进一步的,所述叶轮为涡轮式叶轮,其包括轮芯和叶片,所述叶片沿周向设置于所述轮芯的外表面。叶轮与筛板配合设置,筛板安装在筛板座上,叶轮底面与筛板之间的配合间隙为3-6mm。所述叶轮的轮芯直径为350mm,外径为900mm,轮芯高度为28-35mm。常规叶轮的轮芯直径为520mm,外径为840mm,轮芯高度为148mm。通过减小轮芯尺寸和增大外径尺寸,增大了筛选面积;通过减小轮芯高度,降低了功率消耗,提高了碎解效果,实现了节能降耗。Furthermore, the impeller is a turbine impeller, which includes a wheel core and blades, and the blades are circumferentially arranged on the outer surface of the wheel core. The impeller is arranged in cooperation with the sieve plate, and the sieve plate is installed on the sieve plate seat, and the fitting clearance between the bottom surface of the impeller and the sieve plate is 3-6mm. The wheel core diameter of the impeller is 350mm, the outer diameter is 900mm, and the wheel core height is 28-35mm. The wheel core diameter of a conventional impeller is 520mm, the outer diameter is 840mm, and the wheel core height is 148mm. By reducing the wheel core size and increasing the outer diameter size, the screening area is increased; by reducing the wheel core height, the power consumption is reduced, the crushing effect is improved, and energy saving and consumption reduction are achieved.

与现有叶轮相比,本发明的叶轮轮芯较小,叶片较长,叶片的形状、角度和尺寸经过全面优化。先进的叶轮形式与较大过滤面积的筛板相结合,具有增强碎解作用,改善筛浆能力,提高碎解效能的作用,同时也大大降低了叶轮的能耗。Compared with the existing impeller, the impeller of the present invention has a smaller core, longer blades, and the shape, angle and size of the blades are fully optimized. The advanced impeller form combined with the screen plate with a larger filtering area has the effect of enhancing the crushing effect, improving the pulp screening ability, and improving the crushing efficiency, while also greatly reducing the energy consumption of the impeller.

附图说明BRIEF DESCRIPTION OF THE DRAWINGS

为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据提供的附图获得其他的附图。In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings required for use in the embodiments or the description of the prior art will be briefly introduced below. Obviously, the drawings described below are only embodiments of the present invention. For ordinary technicians in this field, other drawings can be obtained based on the provided drawings without paying creative work.

图1附图为现有水力清洗机结构图;Figure 1 is a structural diagram of a conventional hydraulic cleaning machine;

图2附图为本发明提供的结构示意图;FIG2 is a schematic diagram of the structure provided by the present invention;

图3附图为本发明提供的结构俯视图。FIG. 3 is a top view of the structure provided by the present invention.

其中,1-浆槽,101-第一浆料腔,102-第二浆料腔,2-叶轮,3-良桨出口,4-进桨口,5-重渣出口,6-支撑座,7-驱动电机,8-传动机构,9-筛板座,10-筛板。Among them, 1-slurry trough, 101-first slurry chamber, 102-second slurry chamber, 2-impeller, 3-good paddle outlet, 4-paddle inlet, 5-heavy slag outlet, 6-support seat, 7-drive motor, 8-transmission mechanism, 9-screen plate seat, 10-screen plate.

具体实施方式Detailed ways

下面将对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention are described clearly and completely below. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of them. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.

本发明实施例公开了一种连续式双涡流水力清洗机,清洗机具有浆槽1,浆槽1上开设有进桨口4、重渣出口5和良桨出口3,浆槽1内设置有叶轮2;The embodiment of the present invention discloses a continuous double-vortex hydraulic cleaning machine, which comprises a pulp tank 1, on which a pulp inlet 4, a heavy residue outlet 5 and a good pulp outlet 3 are provided, and an impeller 2 is arranged in the pulp tank 1;

浆槽1内具有筒形的第一浆料腔101和第二浆料腔102,第一浆料腔101的下端与第二浆料腔102的上端连通;第一浆料腔101相对于地面倾斜设置,叶轮2安装于第一浆料腔101的侧壁上端;第二浆料腔102的横截面沿其上端至下端的方向逐渐变小。The slurry tank 1 has a cylindrical first slurry chamber 101 and a second slurry chamber 102, the lower end of the first slurry chamber 101 is connected to the upper end of the second slurry chamber 102; the first slurry chamber 101 is inclined relative to the ground, and the impeller 2 is installed at the upper end of the side wall of the first slurry chamber 101; the cross-section of the second slurry chamber 102 gradually decreases from its upper end to its lower end.

在本发明实施例中,第一浆料腔的中心轴线相对于地面的倾斜角度为45°-55°。In the embodiment of the present invention, the inclination angle of the central axis of the first slurry chamber relative to the ground is 45°-55°.

在本发明实施例中,进桨口4设置于第一浆料腔101靠近下端的侧壁上,良桨出口3设置于第一浆料腔101靠近上端的侧壁上,重渣出口5设置于第二浆料腔102的下端。In an embodiment of the present invention, the paddle inlet 4 is arranged on the side wall of the first slurry chamber 101 near the lower end, the good paddle outlet 3 is arranged on the side wall of the first slurry chamber 101 near the upper end, and the heavy slag outlet 5 is arranged at the lower end of the second slurry chamber 102.

在本发明实施例中,还包括支撑座6,支撑座6一端设置于地面上,另一端与第一浆料腔101和/或第二浆料腔102的外侧壁连接。In the embodiment of the present invention, a support base 6 is further included, one end of the support base 6 is disposed on the ground, and the other end of the support base 6 is connected to the outer side wall of the first slurry chamber 101 and/or the second slurry chamber 102 .

在本发明实施例中,还包括还包括驱动电机7和传动机构8,所述驱动电机7与传动机构8传动连接,所述叶轮2安装在传动机构8上,叶轮2与筛板10配合设置,筛板10安装在筛板座9上,叶轮2底面与筛板10之间的配合间隙为3-6mm。所述叶轮2的轮芯直径为350mm,外径为900mm,轮芯高度为28-35mm。In the embodiment of the present invention, a driving motor 7 and a transmission mechanism 8 are also included. The driving motor 7 is in transmission connection with the transmission mechanism 8. The impeller 2 is mounted on the transmission mechanism 8. The impeller 2 is matched with the sieve plate 10. The sieve plate 10 is mounted on the sieve plate seat 9. The matching clearance between the bottom surface of the impeller 2 and the sieve plate 10 is 3-6 mm. The wheel core diameter of the impeller 2 is 350 mm, the outer diameter is 900 mm, and the wheel core height is 28-35 mm.

在本发明实施例中,叶轮2为涡轮式叶轮2,其包括轮芯和叶片,叶片沿周向设置于轮芯的外表面。In the embodiment of the present invention, the impeller 2 is a turbine impeller 2, which includes a wheel core and blades, and the blades are circumferentially arranged on the outer surface of the wheel core.

本发明提供一种连续式双涡流水力清洗机与现有技术相比,所具有的有益效果是:The present invention provides a continuous double vortex hydraulic cleaning machine, which has the following beneficial effects compared with the prior art:

连续式双涡流水力清洗机对浆槽、叶轮进行全面改进与优化,采用合理的浆槽结构和先进的叶轮形式,加强叶轮的机械作用和搅拌效率;通过浆料在浆槽内形成的双涡流,改善了浆流循环效果和加速了浆液混合速度,降低了流动阻力,从而充分提高设备的碎解效率和产能,降低综合能耗;良浆出口和重杂质出口分别设计在浆槽的上部和下部,能够实现良浆和杂质彻底分离,实现了连续二次碎解处理;The continuous double-vortex hydraulic cleaning machine has comprehensively improved and optimized the pulp tank and impeller, adopted a reasonable pulp tank structure and advanced impeller form, and enhanced the mechanical action and stirring efficiency of the impeller; the double vortex formed by the pulp in the pulp tank improves the pulp flow circulation effect and accelerates the pulp mixing speed, reduces the flow resistance, thereby fully improving the equipment's crushing efficiency and production capacity, and reducing comprehensive energy consumption; the good pulp outlet and heavy impurity outlet are designed at the upper and lower parts of the pulp tank respectively, which can achieve a thorough separation of good pulp and impurities, and realize continuous secondary crushing treatment;

该连续式双涡流水力清洗机与常规水力清洗机相比,节能效率可达25%左右,对相同规格的水力清洗机来说,在同等的碎解度下,可提升产能10-30%。Compared with conventional hydraulic cleaning machines, the continuous double-vortex hydraulic cleaning machine can achieve energy-saving efficiency of about 25%. For hydraulic cleaning machines of the same specifications, the production capacity can be increased by 10-30% at the same crushing degree.

对所公开的实施例的上述说明,使本领域专业技术人员能够实现或使用本发明。对这些实施例的多种修改对本领域的专业技术人员来说将是显而易见的,本文中所定义的一般原理可以在不脱离本发明的精神或范围的情况下,在其它实施例中实现。因此,本发明将不会被限制于本文所示的这些实施例,而是要符合与本文所公开的原理和新颖特点相一致的最宽的范围。The above description of the disclosed embodiments enables those skilled in the art to implement or use the present invention. Various modifications to these embodiments will be apparent to those skilled in the art, and the general principles defined herein may be implemented in other embodiments without departing from the spirit or scope of the present invention. Therefore, the present invention will not be limited to the embodiments shown herein, but rather to the widest scope consistent with the principles and novel features disclosed herein.

Claims (4)

1. The continuous double-vortex hydraulic cleaning machine is provided with a slurry tank (1), wherein a slurry inlet (4), a heavy slag outlet (5) and a good slurry outlet (3) are formed in the slurry tank (1), and an impeller (2) is arranged in the slurry tank; the method is characterized in that: the slurry tank (1) is internally provided with a cylindrical first slurry cavity (101) and a cylindrical second slurry cavity (102), and the lower end of the first slurry cavity (101) is communicated with the upper end of the second slurry cavity (102); the first slurry cavity (101) is obliquely arranged relative to the ground, and the impeller (2) is arranged at the upper end of the side wall of the first slurry cavity (101); the cross section of the second slurry cavity (102) is gradually smaller along the direction from the upper end to the lower end; the vortex flow direction in the first slurry cavity (101) is opposite to the vortex flow direction in the second slurry cavity (102);
the inclination angle of the central axis of the first slurry cavity (101) relative to the ground is 45-55 degrees;
the slurry inlet (4) is arranged on the side wall of the first slurry cavity (101) close to the lower end of the slurry cavity, the good slurry outlet (3) is arranged on the side wall of the first slurry cavity (101) close to the upper end of the slurry cavity, and the heavy slag outlet (5) is arranged at the lower end of the second slurry cavity (102);
the impeller (2) is a turbine impeller (2) and comprises a wheel core and blades, wherein the blades are circumferentially arranged on the outer surface of the wheel core;
wherein the central axis corresponding to the slurry inlet (4) is obliquely arranged relative to the central axis of the first slurry cavity (101).
2. The continuous double-vortex hydraulic cleaning machine according to claim 1, further comprising a supporting seat (6), wherein one end of the supporting seat (6) is arranged on the ground, and the other end is connected with the outer side wall of the first slurry cavity (101) and/or the second slurry cavity (102).
3. The continuous double-vortex hydraulic cleaning machine according to claim 1, further comprising a driving motor (7) and a transmission mechanism (8), wherein the driving motor (7) is in transmission connection with the transmission mechanism (8), and the impeller (2) is mounted on the transmission mechanism (8).
4. A continuous double vortex hydraulic washer according to claim 1 wherein the impeller (2) has a core diameter of 350mm, an outer diameter of 900mm and a core height of 28-35mm.
CN201811544824.XA 2018-12-17 2018-12-17 Continuous double-vortex hydraulic cleaner Active CN109487608B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811544824.XA CN109487608B (en) 2018-12-17 2018-12-17 Continuous double-vortex hydraulic cleaner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811544824.XA CN109487608B (en) 2018-12-17 2018-12-17 Continuous double-vortex hydraulic cleaner

Publications (2)

Publication Number Publication Date
CN109487608A CN109487608A (en) 2019-03-19
CN109487608B true CN109487608B (en) 2024-04-12

Family

ID=65710590

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811544824.XA Active CN109487608B (en) 2018-12-17 2018-12-17 Continuous double-vortex hydraulic cleaner

Country Status (1)

Country Link
CN (1) CN109487608B (en)

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5464161A (en) * 1994-09-30 1995-11-07 The United States Of America As Represented By The Secretary Of The Navy Solid waste pulper
CN1137242A (en) * 1993-12-21 1996-12-04 瑞典商顺智公司 Device for admixing processing agent to pulp suspension
CN2242261Y (en) * 1994-12-30 1996-12-11 山东省诸城市造纸机械厂 High speed double vortex pulp making beater
DE29810276U1 (en) * 1998-06-09 1999-06-02 Voith Sulzer Papiertechnik Patent GmbH, 88213 Ravensburg Screening device for a dirty fiber suspension
JP2005336683A (en) * 2004-05-31 2005-12-08 Niihama Pump Seisakusho:Kk Paper stock-beating pulper
JP2007084968A (en) * 2005-09-22 2007-04-05 Rootaa Kogyo Kk Pulper and rotor
CN102976507A (en) * 2012-11-26 2013-03-20 平桂管理区望高湘桂造纸厂 Wastewater rotational flow treatment device
CN104532638A (en) * 2015-01-05 2015-04-22 南京林业大学 Vertical hydrapulper with drum groove body and spiral backflow plates
CN104870072A (en) * 2012-10-26 2015-08-26 陶氏环球技术有限责任公司 Hydroclone
CN205636330U (en) * 2016-05-12 2016-10-12 潍坊恒德纸业有限公司 Hydrapulper of old and useless thick liquid usefulness made of paper
CN106868906A (en) * 2017-03-02 2017-06-20 胡和萍 A kind of efficient pulper
CN206736621U (en) * 2017-04-29 2017-12-12 姚惠琴 A kind of more vortex differential speed rotation mashing formula beating device for papermaking
CN209722576U (en) * 2018-12-17 2019-12-03 山东晨钟机械股份有限公司 A kind of double vortex waterpower cleaning machines of continous way

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102006008761A1 (en) * 2006-02-24 2007-08-30 Voith Patent Gmbh Process for dissolving and cleaning pulp-containing paper raw materials

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1137242A (en) * 1993-12-21 1996-12-04 瑞典商顺智公司 Device for admixing processing agent to pulp suspension
US5464161A (en) * 1994-09-30 1995-11-07 The United States Of America As Represented By The Secretary Of The Navy Solid waste pulper
CN2242261Y (en) * 1994-12-30 1996-12-11 山东省诸城市造纸机械厂 High speed double vortex pulp making beater
DE29810276U1 (en) * 1998-06-09 1999-06-02 Voith Sulzer Papiertechnik Patent GmbH, 88213 Ravensburg Screening device for a dirty fiber suspension
JP2005336683A (en) * 2004-05-31 2005-12-08 Niihama Pump Seisakusho:Kk Paper stock-beating pulper
JP2007084968A (en) * 2005-09-22 2007-04-05 Rootaa Kogyo Kk Pulper and rotor
CN104870072A (en) * 2012-10-26 2015-08-26 陶氏环球技术有限责任公司 Hydroclone
CN102976507A (en) * 2012-11-26 2013-03-20 平桂管理区望高湘桂造纸厂 Wastewater rotational flow treatment device
CN104532638A (en) * 2015-01-05 2015-04-22 南京林业大学 Vertical hydrapulper with drum groove body and spiral backflow plates
CN205636330U (en) * 2016-05-12 2016-10-12 潍坊恒德纸业有限公司 Hydrapulper of old and useless thick liquid usefulness made of paper
CN106868906A (en) * 2017-03-02 2017-06-20 胡和萍 A kind of efficient pulper
CN206736621U (en) * 2017-04-29 2017-12-12 姚惠琴 A kind of more vortex differential speed rotation mashing formula beating device for papermaking
CN209722576U (en) * 2018-12-17 2019-12-03 山东晨钟机械股份有限公司 A kind of double vortex waterpower cleaning machines of continous way

Also Published As

Publication number Publication date
CN109487608A (en) 2019-03-19

Similar Documents

Publication Publication Date Title
CN111036355B (en) Kitchen garbage pulping device with sand removal function
CN106801455A (en) Garbage treatment device
CN106670918A (en) Environment-friendly cooling equipment for ceramic machining machine
CN109487608B (en) Continuous double-vortex hydraulic cleaner
CN206015401U (en) A kind of new and effective easily defibrator
CN202247504U (en) A New Type of High Consistency Hydrolysis Refiner
CN112127188B (en) Broken paper shredder and broken paper shredding process containing wet strength agent
CN104818635A (en) Eddy kinetic energy gas flow material smashing and material-liquid separation pulping device
CN111335062B (en) Medium-concentration hydraulic pulper
CN209722576U (en) A kind of double vortex waterpower cleaning machines of continous way
CN111424450B (en) High-concentration hydraulic pulper with sieve plate
CN212142332U (en) High-concentration hydraulic pulper
CN213114090U (en) High-efficient pulper
CN205975181U (en) Pulper
CN201447625U (en) Drum Pulper Screening Cleaner
CN212077464U (en) Rotor device of medium-concentration hydraulic pulper
CN213914093U (en) Vertical ball mill
CN201447633U (en) A fiber separator
CN207362589U (en) A kind of continuous pulper of papermaking
CN212077463U (en) Closed cylinder for medium-concentration hydrapulper
CN218756754U (en) Quick dross removal mechanism of paper thick liquid for preparation corrugated surface paper
CN206667392U (en) Garbage treatment device
CN212077462U (en) Energy-saving cutter head of medium-concentration hydraulic pulper
CN210458750U (en) Bipyramid non-centered large-overflow energy-saving hydrapulper
CN212077461U (en) Inclined fine pulp chamber for medium-concentration hydraulic pulper

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
PE01 Entry into force of the registration of the contract for pledge of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: A continuous double vortex hydraulic cleaning machine

Granted publication date: 20240412

Pledgee: Huantai Branch of Industrial and Commercial Bank of China Ltd.

Pledgor: SHANDONG CHENZHONG MACHINERY Co.,Ltd.

Registration number: Y2025980012723