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WO2008134913A1 - Sludge screw vacuum hydroextractor - Google Patents

Sludge screw vacuum hydroextractor Download PDF

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Publication number
WO2008134913A1
WO2008134913A1 PCT/CN2007/001500 CN2007001500W WO2008134913A1 WO 2008134913 A1 WO2008134913 A1 WO 2008134913A1 CN 2007001500 W CN2007001500 W CN 2007001500W WO 2008134913 A1 WO2008134913 A1 WO 2008134913A1
Authority
WO
WIPO (PCT)
Prior art keywords
sludge
screw
dewatering
vacuum
barrel
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.)
Ceased
Application number
PCT/CN2007/001500
Other languages
French (fr)
Chinese (zh)
Inventor
Yueming Xu
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.)
HANGZHOU MEITAI CHEMICAL MACHINERY CO Ltd
Original Assignee
HANGZHOU MEITAI CHEMICAL 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 HANGZHOU MEITAI CHEMICAL MACHINERY CO Ltd filed Critical HANGZHOU MEITAI CHEMICAL MACHINERY CO Ltd
Priority to PCT/CN2007/001500 priority Critical patent/WO2008134913A1/en
Publication of WO2008134913A1 publication Critical patent/WO2008134913A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/121Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
    • C02F11/125Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using screw filters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/11Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
    • B01D29/117Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements arranged for outward flow filtration
    • B01D29/118Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements arranged for outward flow filtration open-ended
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D29/00Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/62Regenerating the filter material in the filter
    • B01D29/64Regenerating the filter material in the filter by scrapers, brushes, nozzles, or the like, acting on the cake side of the filtering element
    • B01D29/6469Regenerating the filter material in the filter by scrapers, brushes, nozzles, or the like, acting on the cake side of the filtering element scrapers
    • B01D29/6476Regenerating the filter material in the filter by scrapers, brushes, nozzles, or the like, acting on the cake side of the filtering element scrapers with a rotary movement with respect to the filtering element
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D35/00Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
    • B01D35/18Heating or cooling the filters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B30PRESSES
    • B30BPRESSES IN GENERAL
    • B30B9/00Presses specially adapted for particular purposes
    • B30B9/02Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
    • B30B9/12Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B30PRESSES
    • B30BPRESSES IN GENERAL
    • B30B9/00Presses specially adapted for particular purposes
    • B30B9/02Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
    • B30B9/12Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing
    • B30B9/121Screw constructions
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/13Treatment of sludge; Devices therefor by de-watering, drying or thickening by heating

Definitions

  • the invention relates to an environmental protection treatment device for sludge. Specifically, it relates to a device for achieving spiral vacuum dehydration of sludge having a moisture content of about 80%.
  • the sludge concentration and dewatering equipment selected by the major sewage treatment plants are basically: horizontal centrifugal dewatering machine, belt pressure filter dewatering machine, plate and frame filter dewatering machine.
  • the "horizontal spiral centrifugal dewatering machine” is the most advanced sludge concentration and dewatering equipment in the world, but the water content of the final sludge after concentration and dewatering in actual operation is still 75%-80%. It is precisely because the sludge after concentrated dewatering still contains relatively high moisture, which brings great difficulties to subsequent sludge disposal.
  • the vulcanized bed is large in volume, high in energy consumption and high in pollution, so the traditional vulcanized bed incineration technology will be phased out.
  • the technical problem to be solved by the present invention is to provide a water retention rate in view of the deficiencies of the prior art.
  • About 80% of the sludge is subjected to secondary dewatering sludge spiral vacuum dewatering machine to make up for the shortage of existing concentrated dewatering equipment, bringing high efficiency, low energy consumption and low pollution process changes for subsequent sludge treatment and disposal. .
  • the present invention employs the following technical solutions: It includes a dewatering device and a sludge feeding device for the dewatering device;
  • the dewatering device includes a dewatering barrel and a combined screw disposed in the barrel, the combined screw including a mandrel and a detachable threaded member and a reverse threaded member alternately arranged outside the mandrel, wherein the combined screw is further provided with a back pressure plate, and the back pressure plate is provided with a hole for the sludge to pass through
  • the barrel wall is provided with a water outlet hole, and the spiral vacuum dehydrator is provided with a vacuum water suction device at the corresponding dewatering hole; the vacuum dewatering unit is further provided with a heating device for the sludge in the dewatering device.
  • the sludge having a water content of about 80% can be subjected to secondary dehydration with low energy consumption and high efficiency, and finally the target of the sludge moisture content within 40% can be achieved. It also brings revolutionary process changes with high efficiency, low energy consumption and low pollution for the subsequent treatment and disposal of sludge.
  • the sludge with a water content of 40% or less is used in the vertical kiln incineration technology, the energy consumption will be greatly reduced. If the sludge with a water content of less than 40% is directly granulated and used as a raw material for combustion in power plants and cement plants, it will be a measure of both economic and social benefits.
  • FIG. 1 is a general schematic diagram of an embodiment of the present invention.
  • FIG. 2 is a schematic exploded view of a combined screw according to an embodiment of the present invention.
  • FIG 3 is a perspective view of a back pressure plate in accordance with an embodiment of the present invention.
  • FIG. 4 is a schematic view of a sludge forced feeding device according to an embodiment of the present invention.
  • Figure 5 is an enlarged cross-sectional view taken along line B of Figure 4 .
  • Figure 6 is a partial schematic view of the barrel of the embodiment of the present invention.
  • Figure 7 is a schematic view of the parts surrounding the water outlet forming a vacuum chamber.
  • Figure 8 is a cross-sectional view of the barrel A-A.
  • Figure 9 is an exploded view of the filter assembly inserted in the water outlet.
  • Fig. 10 is a view taken along line C of Fig. 9. detailed description Refer to the attached drawings.
  • the invention comprises a dewatering device and a sludge forced feeding device of the dewatering device;
  • the dewatering device comprises a dewatering barrel 300 and a combined screw disposed in the barrel, the combined screw comprising a mandrel and being detachably worn a forward conveying screw element 20 and a reverse threading element 22 which are alternately arranged outside the mandrel, and the combined screw is further provided with a back pressure plate 21, and the back pressure plate is provided with a hole 211 through which the sludge passes;
  • the barrel wall is provided with a water outlet hole 24, and the vacuum dewatering machine is provided with a vacuum water suction device at the corresponding dewatering hole; the vacuum dewatering machine is further provided with a heating device for the sludge in the dewatering device.
  • the sludge forced feeding device can be connected to the dewatering barrel and can ensure that the sludge is delivered to the dewatering barrel with a certain pressure.
  • the forced feeding system uses a simple structure: it includes a hopper, the upper portion of the hopper is a cone 4, and the lower portion is a cylinder 5, and the cylindrical hopper is connected to the lower end of the cone hopper.
  • the hopper center is provided with a feeding screw through a fixing bracket. 6.
  • the screw in the cone body is further provided with a large blade for cutting 7.
  • the outer periphery of the thread of the feeding screw is close to the wall of the cylindrical hopper.
  • the feeding blade is designed with a large lead.
  • the outer circumference of the thread of the feeding screw and the single side of the cylindrical hopper wall are kept between 0.3 mm and 0.8 mm.
  • the blanking large blade 7 can be installed on the feeding screw in an angle-adjustable manner, so that it can be adjusted according to different sludges to improve the conveying treatment efficiency.
  • the upper end of the center feeding screw is connected to the variable frequency motor 10 through the thrust pack 9 and the upper and lower flanges 8, and the lower end is kept at a small distance from the first large-diameter conveying screw element 20 of the extrusion screw in the inlet port 11 of the dehydrating barrel. .
  • the variable frequency motor 10 drives the center feeding screw 6 to rotate, which drives the rotation of the rotating blade 7, and generates a pressing force to force the sludge into the barrel.
  • the reaction force generated during the pressing process is absorbed by the thrust pack 9 in the middle of the upper and lower flanges 8.
  • the outer periphery of the thread of the feed screw maintains a small gap with the wall of the hopper during operation to prevent run-up during feeding.
  • the entire feed body is connected to the barrel where the feed port 11 is located through the lower end of the cylindrical hopper 5.
  • the combined screw can be a full rod type with all threads on its surface. In this embodiment, a more reasonable and optimized structure is used.
  • the combined screw includes a mandrel and a threaded member that can be arbitrarily removed and combined outside the mandrel. Further, the mandrel is sleeved with a plurality of threaded elements, the threaded element comprising a threaded element having a forward conveying thread and a threaded element having a reversed thread. In this way, different types of threaded components can be made. In actual production, depending on the sludge to be treated, flexible combination can be made. High processing efficiency and guaranteed dewatering effect.
  • the center of the screw is an integral mandrel 19 with splines engraved on the mandrel 19.
  • the threaded element includes a forward feed threaded element 20 and a reverse threaded element 22.
  • the back pressure plate 21 has an annular shape.
  • One end of the mandrel 19 is connected to the transmission case 3, and the forward conveying screw element 20 and the reverse threading element 22 are alternately sleeved on the mandrel 19 and combined with the back pressure plate to form an adjustable combined screw, and the front end clamping cap 23 is used. locking.
  • the surface of the back pressure cover 21 is engraved with a discharge hole 211 to form a back pressure, and the aperture size is asymmetrically distributed.
  • the thread on the combined screw and the outer periphery of the back pressure plate are close to the wall of the barrel.
  • the gap between the outer circumference of the thread and the back pressure plate and the inner wall of the dewatering barrel is 0.1 mm-0.2 mm.
  • water outlet holes 24 are engraved on the circumference of the barrel at equal intervals, each group engraved with 2-3 discharge water holes, each of which forms a circumference, and each circumference is engraved with 5-20 water outlet holes. twenty four.
  • the outlet opening is located on the circumference of the junction between the forward conveying thread and the reverse thread.
  • a filter device is disposed in the middle of the barrel wall where each set of water outlet holes 24 is located, and a filter screen 25 is disposed in the filter device.
  • the filter net 25 is fixed to the net tray 26 and embedded in the net base 27, and the net base 27 is connected to the fixed interface 28, and the filter device is integrally fixed in the wall of the barrel at the water outlet hole 24.
  • the vacuum suction device includes a vacuum chamber 12 disposed outside the water outlet and a pumping pipe 15 connected to the vacuum chamber.
  • the vacuum chamber 12 is annular and closely attached to the periphery of the water outlet hole, and reference numeral 120 is a part constituting the vacuum chamber.
  • a heater 14 is disposed between each of the two vacuum chambers 12 and is also coated on the outer wall of the barrel.
  • the present invention can be provided with a reverse automatic flushing device that is turned on during the pulse period and flushes the filter screen 25 through a pumping conduit 15 connected to the vacuum chamber.
  • the back pressure plate 21 due to the use of the reverse threaded element 22, the back pressure plate 21, a relatively closed environment will be formed throughout the barrel. Under the condition that the heater 14 is working, when the sludge passes through the barrel, it enters a relatively closed environment in which temperature and pressure act together. According to the characteristics of the sludge, the state of mud-water separation will be achieved under the conditions of temperature and pressure matching. Since the array of water outlet holes 24 is engraved on the barrel, the vacuum system is activated and the moisture is extracted, which is extracted from point to surface and point and surface. Point-to-face extraction The form guarantees the efficiency of dehydration and ensures the dehydration. Moisture first passes through the ring vacuum chamber
  • reference numeral 1 is a stand of the present invention
  • reference numeral 16 is a stand
  • reference numeral 17 is a cooling water pipe
  • reference numeral 18 is a dicing cover.
  • the sludge spiral vacuum dehydrator provided by the present invention is designed according to the physical and chemical characteristics of the sludge.
  • the feed sludge contains up to 80% of water, the sludge itself is particulate and contains a large amount of chemicals such as microorganisms and flocculants, so the flowability of the sludge at normal temperature is very poor, and the present invention passes the forced feeding. Feed into the extrusion screw. In the environment where temperature and pressure are combined, the mud water is automatically separated. According to the principle of low energy consumption of sludge treatment, the moisture in the sludge is separated in liquid form. The specific advantages of this issue are divided into the following points:
  • the large-lead adjustable rotary vane produces a forced downward pressure, and the sludge with extremely poor flow performance is forcibly fed into the extrusion screw.
  • the gap between the rotating blade and the hopper wall is small, which avoids the occurrence of running materials.
  • the variable frequency speed control realizes the control of the infinitely variable speed, ensuring the control of the feeding amount, thereby realizing the efficient operation of the production line.
  • the circumferentially arranged water outlet design of the dewatering barrel enables the vacuuming system to realize the point-to-face extraction form, so that the sludge in the barrel can be uniformly extracted.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Treatment Of Sludge (AREA)

Abstract

A sludge screw vacuum hydroextractor comprises a dewateπng device and a feeding device for the dewateπng device The dewatering device comprises a dewatering drum (300) and a combined screw rod provided therein A right hand screw thread conveying member (20) and a left hand screw thread conveying member (22) are provided in the combined screw rod m an alternating arrangement, and a back pressure plate (21 ) is provided in the combined screw rod, provided with a hole (211) for sludge through therein A drain hole (24) is provided in the drum wall, and a vacuum suction device (13) is provided at the drain hole In addition, a heater (14) isprovided in the lydroextractor for heating the sludge The hydroextractor is used for secondly dewateπng the sludge with about 80% water ratio, finally to attain to the sludge within 40% water ratio

Description

说明书  Instruction manual

一种污泥螺旋式真空脱水机 技术领域 Sludge spiral vacuum dehydrator

本发明涉及污泥环保处理设备。 具体涉及一种将含水率在 80%左右的污泥 实现螺旋式真空脱水的设备。 技术背景  The invention relates to an environmental protection treatment device for sludge. Specifically, it relates to a device for achieving spiral vacuum dehydration of sludge having a moisture content of about 80%. technical background

随着城市污水网络服务的人口不断增加, 水质排放标准的越来越严格以及 城市中各大、 中型污水处理厂的新建或是改扩建, 污泥的产量也迅速增加。就中 国而言, 到 2015年污泥产量将达到 1700万吨 /年, 相当于 2003年的 2倍多。 污 泥如果不被妥善的处理与处置, 将会造成严重的二次污染。 因此, 如何减量、 高 效率、 科学、 无害化地处理污泥己经成为世界各国共同面临的一大难题。 目前, 各大污水处理厂选用的污泥浓缩脱水设备基本为: 卧式离心脱水机、带式压滤脱 水机、 板框式压滤脱水机这三种设备。其中 "卧式螺旋离心脱水机"是目前世界 上较为先进的污泥浓缩脱水设备,但实际运行中最终污泥浓缩脱水后的含水率仍 然在 75%-80%。 正是由于浓缩脱水后的污泥仍然含有相当高的水分, 这给后续 的污泥处置带来了很大的困难。 目前世界各国仍然没有出现革新的处理处置工 艺, 主要还是集中在直接利用硫化床焚烧或立窑焚烧两种技术上。而硫化床体积 大, 能耗高, 污染大, 所以传统硫化床焚烧技术将会被逐步淘汰。 虽然立窑焚烧 技术较硫化床焚烧技术先进, 体积小, 焚烧后污泥含水率很低, 基本完成对污泥 的处理, 但仍面临着高能耗的问题, 无法达到高效率、 低能耗、 减量化处理污泥 的目的。 发明内容  With the increasing population of urban sewage network services, increasingly strict water quality standards, and the construction or expansion of large and medium-sized sewage treatment plants in cities, the production of sludge has also increased rapidly. In the case of China, sludge production will reach 17 million tons per year by 2015, which is more than twice the amount in 2003. If the sludge is not properly disposed and disposed of, it will cause serious secondary pollution. Therefore, how to reduce, efficiently, scientifically and harmlessly treat sludge has become a major problem faced by all countries in the world. At present, the sludge concentration and dewatering equipment selected by the major sewage treatment plants are basically: horizontal centrifugal dewatering machine, belt pressure filter dewatering machine, plate and frame filter dewatering machine. Among them, the "horizontal spiral centrifugal dewatering machine" is the most advanced sludge concentration and dewatering equipment in the world, but the water content of the final sludge after concentration and dewatering in actual operation is still 75%-80%. It is precisely because the sludge after concentrated dewatering still contains relatively high moisture, which brings great difficulties to subsequent sludge disposal. At present, there are still no innovative treatment and disposal processes in countries around the world, mainly focusing on the direct use of two technologies, such as fluidized bed incineration or vertical kiln incineration. The vulcanized bed is large in volume, high in energy consumption and high in pollution, so the traditional vulcanized bed incineration technology will be phased out. Although the vertical kiln incineration technology is more advanced than the vulcanized bed incineration technology, the volume is small, the sludge moisture content after incineration is very low, and the sludge treatment is basically completed, but it still faces the problem of high energy consumption, which cannot achieve high efficiency, low energy consumption, and reduction. Quantify the purpose of sludge treatment. Summary of the invention

本发明所要解决的技术问题是针对现有技术的不足提供一种对含水率在 80%左右的污泥进行二次脱水的污泥螺旋式真空脱水机, 以弥补现有浓缩脱水设 备的不足, 为污泥后续的处理与处置带来高效率、 低能耗、 低污染的工艺变化。 为此, 本发明釆用以下技术方案: 它包括脱水装置及脱水装置的污泥喂料装置; 所述脱水装置包括脱水机筒及设于机筒内的组合式螺杆,所述组合式螺杆包括芯 轴及可拆卸地穿套在芯轴外交替排列的正向输送螺纹元件及反向螺紋元件,所述 组合式螺杆上还设有背压板,所述背压板设有供污泥通过的孔; 所述机筒壁设有 出水孔,所述螺旋真空脱水机在对应脱水孔处设有真空吸水装置; 所述真空脱水 机组还设有对脱水装置中污泥的加热装置。 由于运用本发明的技术方案, 能够低 能耗、高效率地对含水率在 80%左右的污泥进行二次脱水,最终实现污泥含水率 在 40%以内的目标。并为污泥后续的处理与处置带来高效率、低能耗、低污染的 革命性的工艺变化。含水率在 40%以下的污泥釆用立窑焚烧技术时,将大幅度降 低能耗。若含水率在 40%以下的污泥直接制成颗粒后作为发电厂、水泥厂的燃烧 原料, 将是经济与社会效益并举的措施。 附图说明 The technical problem to be solved by the present invention is to provide a water retention rate in view of the deficiencies of the prior art. About 80% of the sludge is subjected to secondary dewatering sludge spiral vacuum dewatering machine to make up for the shortage of existing concentrated dewatering equipment, bringing high efficiency, low energy consumption and low pollution process changes for subsequent sludge treatment and disposal. . To this end, the present invention employs the following technical solutions: It includes a dewatering device and a sludge feeding device for the dewatering device; the dewatering device includes a dewatering barrel and a combined screw disposed in the barrel, the combined screw including a mandrel and a detachable threaded member and a reverse threaded member alternately arranged outside the mandrel, wherein the combined screw is further provided with a back pressure plate, and the back pressure plate is provided with a hole for the sludge to pass through The barrel wall is provided with a water outlet hole, and the spiral vacuum dehydrator is provided with a vacuum water suction device at the corresponding dewatering hole; the vacuum dewatering unit is further provided with a heating device for the sludge in the dewatering device. By using the technical solution of the present invention, the sludge having a water content of about 80% can be subjected to secondary dehydration with low energy consumption and high efficiency, and finally the target of the sludge moisture content within 40% can be achieved. It also brings revolutionary process changes with high efficiency, low energy consumption and low pollution for the subsequent treatment and disposal of sludge. When the sludge with a water content of 40% or less is used in the vertical kiln incineration technology, the energy consumption will be greatly reduced. If the sludge with a water content of less than 40% is directly granulated and used as a raw material for combustion in power plants and cement plants, it will be a measure of both economic and social benefits. DRAWINGS

图 1为本发明所提供实施例的总体示意图。  1 is a general schematic diagram of an embodiment of the present invention.

图 2为本发明所提供实施例的组合式螺杆分解示意图。  2 is a schematic exploded view of a combined screw according to an embodiment of the present invention.

图 3为本发明所提供实施例的背压板的立体图。  3 is a perspective view of a back pressure plate in accordance with an embodiment of the present invention.

图 4为本发明所提供实施例的污泥强制喂料装置的示意图。  4 is a schematic view of a sludge forced feeding device according to an embodiment of the present invention.

图 5为图 4的 B处剖视放大图。  Figure 5 is an enlarged cross-sectional view taken along line B of Figure 4 .

图 6为本发明所提供实施例的机筒局部示意图。  Figure 6 is a partial schematic view of the barrel of the embodiment of the present invention.

图 7为包围在出水孔外构成真空腔的零件的示意图。  Figure 7 is a schematic view of the parts surrounding the water outlet forming a vacuum chamber.

图 8为机筒的 A-A剖面图。  Figure 8 is a cross-sectional view of the barrel A-A.

图 9为插在出水孔中的过滤组件的分解图。  Figure 9 is an exploded view of the filter assembly inserted in the water outlet.

图 10为图 9的 C向视图。 具体实施方式 参照附图。本发明包括脱水装置及脱水装置的污泥强制喂料装置; 所述脱水 装置包括脱水机筒 300及设于机筒内.的组合式螺杆,所述组合式螺杆包括芯轴及 可拆卸地穿套在芯轴外交替排列的正向输送螺纹元件 20及反向螺紋元件 22 , 所 述组合式螺杆上还设有背压板 21, 所述背压板设有供污泥通过的孔 211 ; 所述机 筒壁设有出水孔 24, 所述真空脱水机在对应脱水孔处设有真空吸水装置; 所述 真空脱水机还设有对脱水装置中污泥的加热装置。 Fig. 10 is a view taken along line C of Fig. 9. detailed description Refer to the attached drawings. The invention comprises a dewatering device and a sludge forced feeding device of the dewatering device; the dewatering device comprises a dewatering barrel 300 and a combined screw disposed in the barrel, the combined screw comprising a mandrel and being detachably worn a forward conveying screw element 20 and a reverse threading element 22 which are alternately arranged outside the mandrel, and the combined screw is further provided with a back pressure plate 21, and the back pressure plate is provided with a hole 211 through which the sludge passes; The barrel wall is provided with a water outlet hole 24, and the vacuum dewatering machine is provided with a vacuum water suction device at the corresponding dewatering hole; the vacuum dewatering machine is further provided with a heating device for the sludge in the dewatering device.

污泥强制喂料装置可以采用能与脱水机筒对接,并能保证污泥被具有一定压 力地输送入脱水机筒的装置。在本实施例中,强制喂料系统釆用一种简单的结构: 它包括料斗, 所述料斗的上部为锥形体 4下部为圆柱体 5 , 圆柱体料斗连接于锥 体料斗的下端。 料斗中心通过固定支架设置喂料螺杆 6, 锥形体内的螺杆上还设 有下料大叶片 7, 喂料螺杆的螺紋外周边接近圆柱体料斗壁。 喂料叶片釆用大导 程设计, 一般, 喂料螺杆的螺紋外周边与圆柱体料斗壁单边间隙保持在 0.3mm-0.8mm之间。 所述下料大叶片 7可采用角度可调节的方式安装于在喂料 螺杆上, 这样, 可以根据不同的污泥进行调节, 提高输送处理效率。  The sludge forced feeding device can be connected to the dewatering barrel and can ensure that the sludge is delivered to the dewatering barrel with a certain pressure. In the present embodiment, the forced feeding system uses a simple structure: it includes a hopper, the upper portion of the hopper is a cone 4, and the lower portion is a cylinder 5, and the cylindrical hopper is connected to the lower end of the cone hopper. The hopper center is provided with a feeding screw through a fixing bracket. 6. The screw in the cone body is further provided with a large blade for cutting 7. The outer periphery of the thread of the feeding screw is close to the wall of the cylindrical hopper. The feeding blade is designed with a large lead. Generally, the outer circumference of the thread of the feeding screw and the single side of the cylindrical hopper wall are kept between 0.3 mm and 0.8 mm. The blanking large blade 7 can be installed on the feeding screw in an angle-adjustable manner, so that it can be adjusted according to different sludges to improve the conveying treatment efficiency.

中心喂料螺杆上端通过推力包 9和上下法兰 8与变频电机 10相连接, 下端 与脱水机筒进料口 11中挤压螺杆的第一段大导程输送螺紋元件 20保持较小的距 离。  The upper end of the center feeding screw is connected to the variable frequency motor 10 through the thrust pack 9 and the upper and lower flanges 8, and the lower end is kept at a small distance from the first large-diameter conveying screw element 20 of the extrusion screw in the inlet port 11 of the dehydrating barrel. .

变频电机 10驱动中心喂料螺杆 6旋转, 带动旋转叶片 7的旋转, 产生下压 作用力将污泥强制喂入机筒中。下压过程中所产生的反作用力被上下法兰 8中间 的推力包 9所吸收。喂料螺杆的螺紋外周边在工作过程中与料斗壁保持较小的间 隙, 可防止喂料时产生跑料现象。 整个喂料体通过圆柱体料斗 5 下端与进料口 11所处的机筒相连接。  The variable frequency motor 10 drives the center feeding screw 6 to rotate, which drives the rotation of the rotating blade 7, and generates a pressing force to force the sludge into the barrel. The reaction force generated during the pressing process is absorbed by the thrust pack 9 in the middle of the upper and lower flanges 8. The outer periphery of the thread of the feed screw maintains a small gap with the wall of the hopper during operation to prevent run-up during feeding. The entire feed body is connected to the barrel where the feed port 11 is located through the lower end of the cylindrical hopper 5.

所述组合式螺杆可以是整杆式的, 所有螺紋制于其表面。本实施例釆用了一 种更为合理、优化的结构,所述组合式螺杆包括芯轴及穿套在芯轴外可任意拆卸、 组合的螺纹元件。更进一步地, 所述芯轴上套有多个螺紋元件, 所述螺紋元件包 括制有正向输送螺纹的螺纹元件和制有反向螺纹的螺紋元件。这样, 可以制作不 同型号的螺纹元件, 在实际生产时, 根据所处理的污泥不同, 灵活选择组合, 提 高处理效率并保证脱水效果。 The combined screw can be a full rod type with all threads on its surface. In this embodiment, a more reasonable and optimized structure is used. The combined screw includes a mandrel and a threaded member that can be arbitrarily removed and combined outside the mandrel. Further, the mandrel is sleeved with a plurality of threaded elements, the threaded element comprising a threaded element having a forward conveying thread and a threaded element having a reversed thread. In this way, different types of threaded components can be made. In actual production, depending on the sludge to be treated, flexible combination can be made. High processing efficiency and guaranteed dewatering effect.

如图所示, 螺杆中心为一根整体的芯轴 19, 芯轴 19上刻有花键。 螺紋元件 包括正向输送螺纹元件 20、 反向螺紋元件 22。 所述背压板 21呈环状。 芯轴 19 一端连接于传动箱 3, 正向输送螺纹元件 20、 反向螺紋元件 22交替穿套在芯轴 19上并组合套上背压板组成可调节的组合式螺杆, 前端釆用固定帽 23锁定。 背 压盖板 21表面刻有出料孔 211, 形成背压力, 孔径大小呈不对称分布。 组合式 螺杆上的螺纹及背压板外周边接近机筒壁,一般, 螺紋及背压板外周边与脱水机 筒内壁单边间隙为 0.1mm-0.2mm。 主电机 2驱动时, 传动箱 3传动于组合式螺 杆, 将物料向前推进。 反向螺纹元件 22与背压盖板 21共同产生背压力, ώ于背 压盖板 21表面刻有孔径大小呈不对称分布的出料孔, 即保证了背压力的产生又 能确保物料被顺利向前输送。  As shown, the center of the screw is an integral mandrel 19 with splines engraved on the mandrel 19. The threaded element includes a forward feed threaded element 20 and a reverse threaded element 22. The back pressure plate 21 has an annular shape. One end of the mandrel 19 is connected to the transmission case 3, and the forward conveying screw element 20 and the reverse threading element 22 are alternately sleeved on the mandrel 19 and combined with the back pressure plate to form an adjustable combined screw, and the front end clamping cap 23 is used. locking. The surface of the back pressure cover 21 is engraved with a discharge hole 211 to form a back pressure, and the aperture size is asymmetrically distributed. The thread on the combined screw and the outer periphery of the back pressure plate are close to the wall of the barrel. Generally, the gap between the outer circumference of the thread and the back pressure plate and the inner wall of the dewatering barrel is 0.1 mm-0.2 mm. When the main motor 2 is driven, the transmission case 3 is driven by the combined screw to push the material forward. The reverse threaded element 22 and the back pressure cover 21 together generate a back pressure, and the surface of the back pressure cover 21 is engraved with a discharge hole having an asymmetrically distributed aperture shape, thereby ensuring the generation of back pressure and ensuring smooth material flow. Forward.

参照附图,在机筒圆周上按等分点刻有出水孔 24,每组刻有 2-3排出水孔, 每排出水孔形成一个圆周, 每个圆周上刻有 5-20个出水孔 24。 所述出水孔所处 的位置以处于正向输送螺纹与反向螺纹交界处的圆周上为最好。 每组出水孔 24 所处的机筒壁中间设有过滤装置, 过滤装置中设有过滤网 25。 过滤网 25被固定 在网托 26上并内嵌在网座 27上, 网座 27与固定接口 28相连接, 则过滤装置被 整体固定在出水孔 24处的机筒壁中。  Referring to the drawings, water outlet holes 24 are engraved on the circumference of the barrel at equal intervals, each group engraved with 2-3 discharge water holes, each of which forms a circumference, and each circumference is engraved with 5-20 water outlet holes. twenty four. Preferably, the outlet opening is located on the circumference of the junction between the forward conveying thread and the reverse thread. A filter device is disposed in the middle of the barrel wall where each set of water outlet holes 24 is located, and a filter screen 25 is disposed in the filter device. The filter net 25 is fixed to the net tray 26 and embedded in the net base 27, and the net base 27 is connected to the fixed interface 28, and the filter device is integrally fixed in the wall of the barrel at the water outlet hole 24.

所述真空吸水装置包括设置于出水孔外的真空腔 12, 及与真空腔连接的抽 水管道 15。 真空腔 12呈环形, 紧密贴覆在出水孔的外围, 附图标号 120为构成 真空腔的零件。 在每两个真空腔 12之间设有加热器 14, 同样包覆在机筒外壁。 本发明可设置反向自动冲洗装置,在脉冲时间段内开启,通过与真空腔连接的抽 水管道 15对过滤网 25进行冲洗。  The vacuum suction device includes a vacuum chamber 12 disposed outside the water outlet and a pumping pipe 15 connected to the vacuum chamber. The vacuum chamber 12 is annular and closely attached to the periphery of the water outlet hole, and reference numeral 120 is a part constituting the vacuum chamber. A heater 14 is disposed between each of the two vacuum chambers 12 and is also coated on the outer wall of the barrel. The present invention can be provided with a reverse automatic flushing device that is turned on during the pulse period and flushes the filter screen 25 through a pumping conduit 15 connected to the vacuum chamber.

本发明由于釆用了反向螺纹元件 22,背压板 21, 整个机筒内将形成一个相 对密闭的环境。 在加热器 14工作的条件下, 污泥在机筒内通过时即进入了一种 在温度与压力共同作用的相对密闭环境。根据污泥的特性, 在温度与压力匹配的 条件下将会实现泥水分离的状态。 由于机筒上刻有数组出水孔 24, 此时启动抽 真空系统, 水分将被抽取, 由点到面, 点面结合的方式被抽取。 由点到面的抽取 形式即保证了脱水的效率, 又确保了脱水了均勾度。 水分首先通过环型真空腔In the present invention, due to the use of the reverse threaded element 22, the back pressure plate 21, a relatively closed environment will be formed throughout the barrel. Under the condition that the heater 14 is working, when the sludge passes through the barrel, it enters a relatively closed environment in which temperature and pressure act together. According to the characteristics of the sludge, the state of mud-water separation will be achieved under the conditions of temperature and pressure matching. Since the array of water outlet holes 24 is engraved on the barrel, the vacuum system is activated and the moisture is extracted, which is extracted from point to surface and point and surface. Point-to-face extraction The form guarantees the efficiency of dehydration and ensures the dehydration. Moisture first passes through the ring vacuum chamber

12, 然后进入真空罐 13。 12, then enter the vacuum tank 13.

在图中, 附图标号 1为本发明的机座, 附图标号 16为支架, 附图标号 17为 冷却水管, 附图标号 18为切粒罩。  In the drawings, reference numeral 1 is a stand of the present invention, reference numeral 16 is a stand, reference numeral 17 is a cooling water pipe, and reference numeral 18 is a dicing cover.

本发明所提供的污泥螺旋式真空脱水机,按照污泥的物理与化学特性來完成 设计。进料污泥虽然含有高达 80%的水分,但污泥本身为微粒状并含有大量微生 物与絮凝剂等化学药剂, 因此在常温下污泥的流动性能很差,本发明通过强制喂 料将其送入挤压螺杆中。 在温度与压力配合的环境下, 泥水实现自动分离状态。 根据污泥处理低能耗的原则,污泥中的水分以液态形式分离。本发朋具体优点分 为以下几点:  The sludge spiral vacuum dehydrator provided by the present invention is designed according to the physical and chemical characteristics of the sludge. Although the feed sludge contains up to 80% of water, the sludge itself is particulate and contains a large amount of chemicals such as microorganisms and flocculants, so the flowability of the sludge at normal temperature is very poor, and the present invention passes the forced feeding. Feed into the extrusion screw. In the environment where temperature and pressure are combined, the mud water is automatically separated. According to the principle of low energy consumption of sludge treatment, the moisture in the sludge is separated in liquid form. The specific advantages of this issue are divided into the following points:

1、 大导程可调节式旋转叶片产生强制下压的作用力, 把流动性能极差的污 泥强制喂入挤压螺杆中。 旋转叶片与料斗壁的间隙小, 避免了跑料现象的发生。 变频调速实现了无极变速的控制,确保喂料量的控制, 从而实现生产线的高效运 转。  1. The large-lead adjustable rotary vane produces a forced downward pressure, and the sludge with extremely poor flow performance is forcibly fed into the extrusion screw. The gap between the rotating blade and the hopper wall is small, which avoids the occurrence of running materials. The variable frequency speed control realizes the control of the infinitely variable speed, ensuring the control of the feeding amount, thereby realizing the efficient operation of the production line.

2、 可调节的组合式螺杆设计, 反向螺纹元件与输送螺纹元件的完美组合在 机筒内实现了相对密闭的环境。为确保在反向作用力的影响下,机筒内的污泥仍 然能被向前输送, 设置了背压盖板, 即保证顺利输送, 又形成相对压力。 根据螺 纹元件的不同组合,将实现脱水量的控制。避免生产线完全被固定在单一的脱水 率数值上。  2. Adjustable combined screw design, the perfect combination of reverse threaded elements and threaded threaded elements creates a relatively closed environment within the barrel. In order to ensure that the sludge in the barrel can still be transported forward under the influence of the reverse force, a back pressure cover is provided, which ensures smooth delivery and relative pressure. The control of the amount of dewatering will be achieved depending on the different combinations of the thread elements. Avoid the line being completely fixed to a single dewatering rate value.

3、在加热器传热后,机筒内部将实现温度与压力共同作用的相对密闭环境, 泥水实现分离状态。  3. After the heat transfer of the heater, the inside of the barrel will realize a relatively closed environment in which temperature and pressure work together, and the muddy water will be separated.

4、 脱水机筒的圆周排列式出水口设计, 使得抽真空系统实现了由点到面的 抽取形式, 使机筒内的污泥能被均匀的抽取水分。  4. The circumferentially arranged water outlet design of the dewatering barrel enables the vacuuming system to realize the point-to-face extraction form, so that the sludge in the barrel can be uniformly extracted.

5、 脉冲反冲洗装置被完成设定后, 在固定时间间隔内对过滤网进行清洗, 确保过滤网的通畅, 使脱水能连续式进行。  5. After the pulse backwashing device is set, clean the filter in a fixed time interval to ensure the smoothness of the filter, so that the dehydration can be carried out continuously.

Claims

权利要求书 Claim 1、 一种污泥螺旋式真空脱水机, 其特征在于它包括脱水装置及脱水装置的 污泥强制喂料装置; 所述脱水装置包括脱水机筒及设于机筒内 '的组合式螺杆,所 述组合式螺杆包括芯轴及可拆卸地穿套在芯轴外交替排列的正向输送螺纹元件 及反向螺紋元件,所述组合式螺杆上还设有背压板,所述背压板设有供污泥通过 的孔; 所述机筒壁设有出水孔,所述螺旋式真空脱水机在对应脱水孔处设有真空 吸水装置; 所述螺旋式真空脱水机还设有对脱水装置中污泥的加热装置。 A sludge spiral vacuum dewatering machine, characterized in that it comprises a dewatering device and a sludge forced feeding device of a dewatering device; the dewatering device comprises a dewatering barrel and a combined screw disposed in the barrel; The combined screw includes a mandrel and a forward conveying threaded member and a reverse threaded member which are detachably arranged outside the mandrel, and the combined screw is further provided with a back pressure plate, and the back pressure plate is provided with a hole for the sludge to pass through; the barrel wall is provided with a water outlet hole, and the spiral vacuum dewatering machine is provided with a vacuum water absorption device at the corresponding dewatering hole; the spiral vacuum dewatering machine is further provided with a sewage in the dewatering device Mud heating device. 2、 如权利要求 1所述的一种污泥螺旋式真空脱水机, 其特征在于所述背压 板呈环状。  2. A sludge screw vacuum dewatering machine according to claim 1 wherein said back pressure plate is annular. 3、 如权利要求 1或 2所述的一种污泥螺旋式真空脱水机, 其特征在于组合 式螺杆上的螺纹及背压板的外周边接近机筒壁。  3. A sludge screw vacuum dewatering machine according to claim 1 or 2, wherein the threads on the combined screw and the outer periphery of the back pressure plate are adjacent to the barrel wall. 4、 如权利要求 1或 2所述的一种污泥螺旋式真空脱水机, 其特征在于所述 出水孔处于正向输送螺纹与反向螺纹交界处的圆周上。  A sludge spiral vacuum dehydrator according to claim 1 or 2, wherein said water outlet hole is on a circumference of a boundary between a forward conveying thread and a reverse thread. 5、 如权利要求 1或 2所述的一种污泥螺旋式真空脱水机, 其特征在于所述 加热装置为包覆在机筒外的加热器。  A sludge spiral vacuum dehydrator according to claim 1 or 2, wherein said heating means is a heater coated outside the barrel. 6、 如权利要求 1或 2所述的一种污泥螺旋式真空脱水机, 其特征在于所述 真空吸水装置包括设置于出水孔外的真空腔及与真空腔连接的抽水管道;所述出 水孔处设有过滤装置。  6. The sludge screw vacuum dewatering machine according to claim 1 or 2, wherein the vacuum suction device comprises a vacuum chamber disposed outside the water outlet hole and a pumping pipe connected to the vacuum chamber; A filtering device is provided at the hole. .  . 7、 如权利要求 1或 2所述的一种污泥螺旋式真空脱水机, 其特征在于所述 污泥强制喂料装置包括料斗,所述料斗的上部为锥形体下部为圆柱体,料斗中心 设置喂料螺杆,锥形体内的螺杆上还设有下料大叶片, 喂料螺杆的螺纹外周边接 近圆柱体料斗壁。 7. A sludge spiral vacuum dewatering machine according to claim 1 or 2, wherein said sludge forced feeding device comprises a hopper, and the upper portion of said hopper is a cylindrical body at the lower part of the cone, the center of the hopper The feeding screw is arranged, and the screw in the cone body is further provided with a large blade for cutting, and the outer periphery of the thread of the feeding screw is close to the wall of the cylindrical hopper. 8、 如权利要求 7所述的一种污泥螺旋式真空脱水机, 其特征在于所述下料 大叶片角度可调节地安装于喂料螺杆上。  8. A sludge screw vacuum dewatering machine according to claim 7, wherein said blanking large blade angle is adjustably mounted to the feed screw.
PCT/CN2007/001500 2007-05-08 2007-05-08 Sludge screw vacuum hydroextractor Ceased WO2008134913A1 (en)

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CN107459245A (en) * 2017-09-04 2017-12-12 池云飞 A kind of method that bipacking-auger sludge conveyer is dehydrated to sludge
JP2021122815A (en) * 2020-02-10 2021-08-30 水ing株式会社 Screw press and its operation method
JP7444626B2 (en) 2020-02-10 2024-03-06 水ing株式会社 Screw press and its operating method
CN118087437A (en) * 2024-04-28 2024-05-28 星原建设集团有限公司 Road surface ponding mud cleaning device

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