CN206767899U - A high calcium water treatment system - Google Patents
A high calcium water treatment system Download PDFInfo
- Publication number
- CN206767899U CN206767899U CN201720587032.5U CN201720587032U CN206767899U CN 206767899 U CN206767899 U CN 206767899U CN 201720587032 U CN201720587032 U CN 201720587032U CN 206767899 U CN206767899 U CN 206767899U
- Authority
- CN
- China
- Prior art keywords
- calcium
- mixing tank
- tank
- treatment system
- decalcification
- 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
Links
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
Description
技术领域technical field
本实用新型涉及制浆造纸废水处理系统,特别涉及一种制浆造纸废水的除钙装置。The utility model relates to a pulping and papermaking wastewater treatment system, in particular to a decalcification device for pulping and papermaking wastewater.
背景技术Background technique
在制浆造纸生产过程中,废纸原料以及造纸的涂布、加填等工序均含有或大量使用碳酸钙,因此造纸废水中钙化物含量非常高,由于微生物的作用,废水中的有机物易转化为挥发性的脂肪酸等物质,其与碳酸钙发生反应,使得钙从沉淀物转化成离子态,进入制浆造纸废水中,如果不降低造纸废水中的钙离子,后序废水处理系统中的管道非常容易结垢,影响设备的正常使用。In the process of pulping and papermaking, waste paper raw materials and papermaking processes such as coating and filling all contain or use a large amount of calcium carbonate. Therefore, the calcium content in papermaking wastewater is very high. Due to the action of microorganisms, organic matter in wastewater is easily transformed. It is a volatile fatty acid and other substances, which react with calcium carbonate, so that the calcium is converted from the precipitate into an ion state, and enters the pulp and paper wastewater. If the calcium ion in the paper wastewater is not reduced, the pipeline in the subsequent wastewater treatment system It is very easy to scale and affect the normal use of equipment.
发明内容Contents of the invention
本实用新型的目的在于,解决高钙水进入废水处理系统容易结垢,堵塞管道等技术弊端,提出了一种高钙水处理系统,包括:除钙混合池、安装于除钙混合池内的搅拌机、分别与除钙混合池连通的高钙废水池和厌氧反应器、安装在厌氧回流水管路上的流量计、连接于除钙混合池出口的提升泵、连接于提升泵的斜网过滤装置、设置在斜网过滤装置下方的浆池。The purpose of this utility model is to solve the technical disadvantages of high-calcium water entering the waste water treatment system, such as easy scaling and blockage of pipelines, and proposes a high-calcium water treatment system, including: a decalcification mixing tank, a mixer installed in the decalcification mixing tank , the high-calcium waste water tank and the anaerobic reactor respectively connected with the decalcification mixing tank, the flow meter installed on the anaerobic return water pipeline, the lift pump connected to the outlet of the decalcification mixing tank, and the inclined screen filter device connected to the lift pump , The pulp pool set under the inclined screen filter device.
进一步地,上述厌氧反应器中的厌氧回流水靠厌氧反应器与除钙混合池之间的高程差自流到除钙混合池中。Further, the anaerobic return water in the above-mentioned anaerobic reactor flows into the decalcification mixing tank by virtue of the elevation difference between the anaerobic reactor and the decalcification mixing tank.
进一步地,经过所述斜网过滤装置过滤后的清水经出水管进入废水收集池。Further, the clean water filtered by the inclined screen filter device enters the waste water collection tank through the outlet pipe.
进一步地,所述浆池中的沉淀物和纸浆经过压滤后用于造纸,清水经过管道进入废水收集池。Further, the sediment and pulp in the pulp tank are used for papermaking after being press-filtered, and the clean water enters the waste water collection tank through pipelines.
进一步地,所述斜网过滤装置与浆池之间安装有排渣阀。Further, a slag discharge valve is installed between the inclined screen filter device and the pulp tank.
本实用新型的技术效果在于:厌氧回流水中含有大量的碳酸根和碳酸氢根离子,当高钙废水与厌氧回流水在除钙混合池中混合时发生化学反应产生含有碳酸钙成分的钒花絮体,其中搅拌机加快了它们之间的混合和化学反应,再经过斜网过滤装置的过滤,将造纸废水中的沉淀物与清水分离,通过定期开启排渣阀可以将沉淀物排到浆池中,浆池中的沉淀物和纸浆再经过压滤后可用于造纸,因此排放到废水收集池的废液中钙离子及碳酸钙显著降低,减少了后序废水处理工段结垢的几率,同时还实现了资源的循环利用。The technical effect of the utility model is that: the anaerobic reflux water contains a large amount of carbonate and bicarbonate ions, when the high-calcium wastewater and the anaerobic reflux water are mixed in the decalcification mixing tank, a chemical reaction occurs to produce vanadium containing calcium carbonate. The floc, in which the mixer speeds up the mixing and chemical reaction between them, and then passes through the inclined screen filter device to separate the sediment in the papermaking wastewater from the clean water, and the sediment can be discharged to the slurry tank by regularly opening the slag discharge valve In the process, the sediment and pulp in the slurry tank can be used for papermaking after pressure filtration, so the calcium ions and calcium carbonate in the waste liquid discharged to the wastewater collection tank are significantly reduced, reducing the scaling probability of the subsequent wastewater treatment section, and at the same time It also realizes the recycling of resources.
流量计可以监控厌氧回流水的加入量,确保其加入量和含钙废水的加入量相互匹配,如果加入的太少不能彻底中和钙离子,加入量太多,造成浪费。The flow meter can monitor the amount of anaerobic reflux water added to ensure that its added amount matches the amount of calcium-containing wastewater added. If too little is added, calcium ions cannot be completely neutralized, and too much added will cause waste.
附图说明Description of drawings
图1是高钙水处理系统的结构示意图。Figure 1 is a schematic diagram of the structure of a high calcium water treatment system.
具体实施方式detailed description
以下将结合附图,对本实用新型的实施例进行详细描述。Embodiments of the present utility model will be described in detail below in conjunction with the accompanying drawings.
实施例一Embodiment one
图1是高钙水处理系统的结构示意图,该高钙水处理系统,包括:除钙混合池1、安装于除钙混合池1内的搅拌机2、分别与除钙混合池1连通的高钙废水池3和厌氧反应器4、安装在厌氧回流水管路上的流量计5、连接于除钙混合池1出口的提升泵6、与提升泵6连接的斜网过滤装置7、设置在斜网过滤装置7下方的浆池8,安装于斜网过滤装置7与浆池8之间的排渣阀9。经过斜网过滤装置7过滤后的清水经出水管进入废水收集池10,浆池8中的沉淀物和纸浆经过压滤后用于造纸,清水经过管道进入废水收集池10。Fig. 1 is a structural schematic diagram of a high-calcium water treatment system. The high-calcium water treatment system includes: a decalcification mixing tank 1, a mixer 2 installed in the decalcification mixing tank 1, and a high-calcium decalcification mixing tank 1 communicated with the decalcification mixing tank 1 respectively. Wastewater tank 3 and anaerobic reactor 4, flow meter 5 installed on the anaerobic return water pipeline, lift pump 6 connected to the outlet of decalcification mixing tank 1, inclined screen filter device 7 connected with lift pump 6, arranged on the inclined The pulp tank 8 below the screen filter device 7 is installed on the slag discharge valve 9 between the inclined screen filter device 7 and the pulp tank 8 . The clear water filtered by the inclined screen filter device 7 enters the waste water collection tank 10 through the outlet pipe.
该处理系统工作时,高钙废水与厌氧回流水在除钙混合池1中混合时发生化学反应产生含有碳酸钙成分的钒花絮体,其中搅拌机2加快了它们之间的混合和化学反应,在此过程中流量计5监控厌氧回流水的加入量,使其加入量和高钙废水的加入量相匹配,确保钙离子被完全中和,提升泵6将发生化学反应后的造纸废水抽送到斜网过滤装置7,经过斜网过滤装置7的过滤,将造纸废水中的沉淀物与清水分离,通过定期开启排渣阀9可以将沉淀物排到浆池8中,浆池8中的沉淀物和纸浆再经过压滤后可用于造纸,因此排放到废水收集池10的废液中钙离子及碳酸钙显著降低,减少了后序废水处理工段结垢的几率,同时还实现了资源的循环利用。When the treatment system is working, a chemical reaction occurs when the high-calcium wastewater and anaerobic reflux water are mixed in the decalcification mixing tank 1 to produce vanadium flocs containing calcium carbonate, and the mixer 2 speeds up the mixing and chemical reaction between them. During this process, the flow meter 5 monitors the amount of anaerobic reflux water to match the amount of high-calcium wastewater to ensure that the calcium ions are completely neutralized, and the lift pump 6 pumps the papermaking wastewater after the chemical reaction to the inclined screen filter device 7, through the filtration of the inclined screen filter device 7, the sediment in the papermaking wastewater is separated from the clear water, and the sediment can be discharged into the pulp tank 8 by regularly opening the slag discharge valve 9, and the sediment in the pulp tank 8 The sediment and pulp can be used for papermaking after pressure filtration, so the calcium ions and calcium carbonate in the waste liquid discharged into the waste water collection tank 10 are significantly reduced, reducing the chance of fouling in the subsequent waste water treatment section, and realizing resource conservation at the same time Recycling.
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720587032.5U CN206767899U (en) | 2017-05-24 | 2017-05-24 | A high calcium water treatment system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720587032.5U CN206767899U (en) | 2017-05-24 | 2017-05-24 | A high calcium water treatment system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206767899U true CN206767899U (en) | 2017-12-19 |
Family
ID=60639418
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201720587032.5U Active CN206767899U (en) | 2017-05-24 | 2017-05-24 | A high calcium water treatment system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206767899U (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108107935A (en) * | 2017-12-25 | 2018-06-01 | 湖南汇科技术咨询有限公司 | Soilless culture intelligent nutrition liquid circulation-supplied system |
CN110054352A (en) * | 2019-04-17 | 2019-07-26 | 安徽建筑大学 | A method of utilizing calcium ion in ASBR technique removal waste incineration and generating electricity percolate |
CN110204094A (en) * | 2019-06-05 | 2019-09-06 | 南京化工园博瑞德水务有限公司 | A kind of high calcium water treatment system |
WO2021047059A1 (en) * | 2019-09-10 | 2021-03-18 | 同济大学 | Method for removing calcium ions from high-concentration organic wastewater |
CN112830599A (en) * | 2021-01-07 | 2021-05-25 | 北京朗新明环保科技有限公司 | Coal-electricity integrated wastewater pretreatment device and method |
CN114671529A (en) * | 2022-03-03 | 2022-06-28 | 广西大学 | Novel method for removing calcium by microorganism-induced calcium carbonate precipitation before anaerobic treatment of high-calcium organic wastewater |
-
2017
- 2017-05-24 CN CN201720587032.5U patent/CN206767899U/en active Active
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108107935A (en) * | 2017-12-25 | 2018-06-01 | 湖南汇科技术咨询有限公司 | Soilless culture intelligent nutrition liquid circulation-supplied system |
CN110054352A (en) * | 2019-04-17 | 2019-07-26 | 安徽建筑大学 | A method of utilizing calcium ion in ASBR technique removal waste incineration and generating electricity percolate |
CN110054352B (en) * | 2019-04-17 | 2021-11-19 | 安徽建筑大学 | Method for removing calcium ions in garbage incineration power generation leachate by using ASBR (anaerobic sequencing batch reactor) process |
CN110204094A (en) * | 2019-06-05 | 2019-09-06 | 南京化工园博瑞德水务有限公司 | A kind of high calcium water treatment system |
WO2021047059A1 (en) * | 2019-09-10 | 2021-03-18 | 同济大学 | Method for removing calcium ions from high-concentration organic wastewater |
US11999642B2 (en) | 2019-09-10 | 2024-06-04 | Tongji University | Method for removing calcium ions from high concentration organic wastewater |
CN112830599A (en) * | 2021-01-07 | 2021-05-25 | 北京朗新明环保科技有限公司 | Coal-electricity integrated wastewater pretreatment device and method |
CN114671529A (en) * | 2022-03-03 | 2022-06-28 | 广西大学 | Novel method for removing calcium by microorganism-induced calcium carbonate precipitation before anaerobic treatment of high-calcium organic wastewater |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN206767899U (en) | A high calcium water treatment system | |
CN205874071U (en) | Thermal power plant contains coal effluent disposal system | |
CN101219837B (en) | Ozonation process and equipment for oil-containing alkali wastewater | |
CN105366893A (en) | A printing and dyeing wastewater treatment system and method | |
CN103880204A (en) | Method for removing nickel ions from electroplating sewage | |
CN103011462B (en) | Device and method for treating waste residues of circulating make-up water by reutilizing lime softening method of power plant | |
CN201136828Y (en) | Ozone treatment system for oil-containing alkaline waste water | |
CN203700087U (en) | Mine shaft wastewater purification treatment device | |
CN205258202U (en) | Pharmaceutical chemical engineering effluent treatment plant | |
CN202297284U (en) | Automatic control device for clean water treatment | |
CN205258241U (en) | Printing and dyeing wastewater treatment system | |
CN204848593U (en) | Be used for dedicated sewage treatment system between numerical control processing vehicle | |
CN106745966A (en) | A kind of steel wastewater and the device of municipal wastewater mixed regeneration reuse | |
CN213446615U (en) | Ethylene-vinyl acetate copolymer adhesive wastewater treatment device | |
CN206203967U (en) | A kind of sewage plant tail water enhanced flocculation and sloping plate deposition coupled processing system | |
CN203653367U (en) | Hydrochloric acid wastewater treatment equipment | |
CN104386855A (en) | Method for preventing membrane filtration concentrated liquid from being scaled | |
CN205188014U (en) | Wet flue gas desulfurization effluent treatment plant of thermal power plant | |
CN211170202U (en) | Sewage treatment device | |
CN204174041U (en) | A kind of biochemical waste water treatment unit | |
CN203284277U (en) | Modularized water purifier | |
CN209428280U (en) | A kind of miniature coating wastewater Processing Equipment | |
CN111635069A (en) | A kind of bone gelatin wastewater treatment and reuse device and its process | |
CN204848513U (en) | Sewage purifier | |
CN205398301U (en) | Full -automatic high -efficient water purification system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |