WO2017143806A1 - Glass device for recovering and multilevel processing chemical waste water - Google Patents
Glass device for recovering and multilevel processing chemical waste water Download PDFInfo
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- WO2017143806A1 WO2017143806A1 PCT/CN2016/105689 CN2016105689W WO2017143806A1 WO 2017143806 A1 WO2017143806 A1 WO 2017143806A1 CN 2016105689 W CN2016105689 W CN 2016105689W WO 2017143806 A1 WO2017143806 A1 WO 2017143806A1
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- the present invention relates to the field of glass devices, and more particularly to a glass device for recycling and multi-stage treatment of chemical wastewater.
- the technical problem mainly solved by the invention is to provide a glass device for recycling and multi-stage treatment of chemical waste water, which is purified by multi-stage treatment by solid-liquid, and has strong pertinence, thorough purification, convenient treatment, high efficiency, safety and practicability. It has broad market prospects for the recycling of chemical wastewater and the popularization of multi-stage processing glass devices.
- the present invention provides a glass apparatus for recycling and multi-stage treatment of chemical wastewater, comprising: a plurality of recovery devices, a standing device, a first solid processing device, a second solid processing device, and a first liquid treatment a device, a second liquid processing device, and a collecting device, wherein the plurality of recycling devices are respectively connected to the stationary device, and the first solid processing device is connected to the bottom of the stationary device through a first two-way valve, a second solid processing device is connected to the output end of the first solid processing device, and the first liquid processing device is connected to a side of the upper portion of the stationary device via a second two-way valve, the second liquid processing device Connected to an output end of the first liquid processing device, and the second solid processing device and the output end of the second liquid processing device are respectively connected The collecting device.
- the openings of the plurality of recovery devices are sequentially increased radially away from the stationary device.
- the resting device has a circular cross-sectional shape.
- the cross-sectional diameter of the rest device is sequentially increased from the middle to the both ends of the rest device.
- the top of the first solids processing device is provided with a shower device or a drip device.
- the shower device or the drip device is provided with dilute hydrochloric acid, dilute nitric acid, dilute sulfuric acid, sodium hydroxide, potassium hydroxide, sodium carbonate or sodium hydrogencarbonate.
- the second solid processing apparatus is provided with a filtering device having a pore diameter of less than 0.1 mm.
- the first liquid processing apparatus is provided with a carbonaceous mesh having a thickness greater than 2 mm.
- an ion exchange membrane is disposed within the second liquid processing apparatus.
- the collection device is spherical.
- the invention has the beneficial effects that the invention is used for the recovery of chemical wastewater and the multi-stage treatment glass device is purified by multi-stage treatment by solid-liquid, and has strong pertinence, thorough purification, convenient treatment, high efficiency, safety and practicability, and is used in chemistry. Wastewater recovery and multi-stage treatment of glass equipment There is a broad market prospect.
- FIG. 1 is a schematic view showing the structure of a preferred embodiment of a multi-stage processing glass apparatus for recovering chemical waste water according to the present invention.
- an embodiment of the present invention includes:
- a recycling and multi-stage processing glass device for chemical wastewater comprising: a plurality of recovery devices 2, a standing device 1, a first solid processing device 3, a second solid processing device 4, a first liquid processing device 5, and a second Liquid treatment device 6 and collection device 7.
- the plurality of recovery devices 2 are respectively connected to the stationary device 1 to allow the wastewater to stand in the stationary device 1 for a period of time to achieve stratification, and the first solid processing device 3 is connected through the first two-way valve.
- the bottom of the stationary device 1 opens the first two-way valve when the sedimentation wastewater at the bottom needs to be treated, and the second solid processing device 4 is connected
- the output end of the first solid processing device 3, the settled wastewater is purified by the first solid processing device 3 and the second solid processing device 4, respectively, and the first liquid processing device 5 passes through the second two-way valve Connecting the side of the upper portion of the stationary device 1 to open the second two-way valve when the upper layer wastewater needs to be treated, and the second liquid processing device 6 is connected to the output end of the first liquid processing device 5
- the upper layer wastewater is subjected to purification treatment via the first liquid processing device 5 and the second liquid processing device 6, respectively, and the second solid processing device 4 and the output end of the second liquid processing device 6 are respectively connected to the collection.
- the opening ports of the plurality of recovery devices 2 are sequentially increased radially away from the direction of the stationary device 1 to facilitate pouring and preventing leakage.
- the standing device 1 has a circular cross section shape.
- the cross-sectional diameter of the stationary device 1 is sequentially increased from the middle to the both ends of the stationary device 1 to facilitate stratification of the wastewater.
- the top of the first solid processing device 3 is provided with a shower device or a drip device.
- the shower device or the drip device is provided with dilute hydrochloric acid, dilute nitric acid, dilute sulfuric acid, sodium hydroxide, potassium hydroxide, sodium carbonate or sodium hydrogencarbonate, and is selected by spraying or dripping the sedimentation wastewater.
- dilute hydrochloric acid dilute nitric acid
- dilute sulfuric acid sodium hydroxide, potassium hydroxide, sodium carbonate or sodium hydrogencarbonate
- An acidic liquid or an alkaline liquid that utilizes a chemical reaction to remove solid deposits that are poorly soluble in water.
- the second solid processing device 4 is provided with a filtering device 401 having a pore diameter of less than 0.1 mm, and the solid residue is performed by the filtering device 401. Filter to further separate the solids.
- the first liquid processing device 5 is provided with a carbonaceous mesh 501 having a thickness greater than 2 mm, and the charcoal is favorable for adsorbing foreign matter.
- the second liquid processing device 6 is provided with an ion exchange membrane 601 for separating ions dissolved in water.
- the collection device 7 is spherical.
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Abstract
Disclosed is a glass device for the recovering and multilevel processing of chemical waste water, including: several recovery devices (2), a standing device (1), a first solid processing device (3), a second solid processing device (4), a first liquid processing device (5), a second liquid processing device (6) and a collection device (7), wherein the several recovery devices (2) are respectively connected in communication to the standing device (1), the first solid processing device (3) is connected in communication to the bottom of the standing device (1), and the first liquid processing device (5) is connected in communication to the side on the upper portion of the standing device (1). By the above-mentioned way, in the glass device for recovering and multilevel processing chemical waste water, solids and liquids are purified by multilevel processing, respectively, such that the pertinence is strong, the purification is thorough, the processing is convenient, the efficiency is high, and the glass device is safe and practical. The glass device has an extensive market prospect in the popularization of a glass device for the recovering and multilevel processing of chemical waste water.
Description
本发明涉及玻璃装置领域，特别是涉及一种用于化学废水的回收及多级处理玻璃装置。The present invention relates to the field of glass devices, and more particularly to a glass device for recycling and multi-stage treatment of chemical wastewater.
在化学实验中会产生大量的混合型废水，其特点为物质种类复杂且物质形态多样，并且大多具有难溶解或者具有腐蚀性，如果直接将其排出会对管道设施以及自然环境造成较大的危害。In chemical experiments, a large amount of mixed wastewater is produced, which is characterized by complex material types and various material forms, and most of them are difficult to dissolve or corrosive. If they are directly discharged, they will cause great harm to pipeline facilities and the natural environment. .
发明内容Summary of the invention
本发明主要解决的技术问题是提供一种用于化学废水的回收及多级处理玻璃装置，通过固液分别多级处理净化，针对性强、净化彻底、处理方便、效率高、安全实用，在用于化学废水的回收及多级处理玻璃装置的普及上有着广泛的市场前景。The technical problem mainly solved by the invention is to provide a glass device for recycling and multi-stage treatment of chemical waste water, which is purified by multi-stage treatment by solid-liquid, and has strong pertinence, thorough purification, convenient treatment, high efficiency, safety and practicability. It has broad market prospects for the recycling of chemical wastewater and the popularization of multi-stage processing glass devices.
为解决上述技术问题，本发明提供一种用于化学废水的回收及多级处理玻璃装置，包括：若干回收装置、静置装置、第一固体处理装置、第二固体处理装置、第一液体处理装置、第二液体处理装置和收集装置，所述若干回收装置分别连通连接所述静置装置，所述第一固体处理装置通过第一二通阀连通连接所述静置装置的底部，所述第二固体处理装置连通连接所述第一固体处理装置的输出端，所述第一液体处理装置通过第二二通阀连通连接所述静置装置的上部的侧面，所述第二液体处理装置连通连接所述第一液体处理装置的输出端，所述第二固体处理装置与所述第二液体处理装置的输出端分别连通连接
所述收集装置。In order to solve the above technical problems, the present invention provides a glass apparatus for recycling and multi-stage treatment of chemical wastewater, comprising: a plurality of recovery devices, a standing device, a first solid processing device, a second solid processing device, and a first liquid treatment a device, a second liquid processing device, and a collecting device, wherein the plurality of recycling devices are respectively connected to the stationary device, and the first solid processing device is connected to the bottom of the stationary device through a first two-way valve, a second solid processing device is connected to the output end of the first solid processing device, and the first liquid processing device is connected to a side of the upper portion of the stationary device via a second two-way valve, the second liquid processing device Connected to an output end of the first liquid processing device, and the second solid processing device and the output end of the second liquid processing device are respectively connected
The collecting device.
在本发明一个较佳实施例中，所述若干回收装置的开口口径向远离所述静置装置的方向依次增大。In a preferred embodiment of the invention, the openings of the plurality of recovery devices are sequentially increased radially away from the stationary device.
在本发明一个较佳实施例中，所述静置装置的横截面形状为圆形。In a preferred embodiment of the invention, the resting device has a circular cross-sectional shape.
在本发明一个较佳实施例中，所述静置装置的横截面直径由所述静置装置的中间向两端的方向依次增大。In a preferred embodiment of the invention, the cross-sectional diameter of the rest device is sequentially increased from the middle to the both ends of the rest device.
在本发明一个较佳实施例中，所述第一固体处理装置的顶部设置有喷淋装置或者滴液装置。In a preferred embodiment of the invention, the top of the first solids processing device is provided with a shower device or a drip device.
在本发明一个较佳实施例中，所述喷淋装置或者所述滴液装置内放置稀盐酸、稀硝酸、稀硫酸、氢氧化钠、氢氧化钾、碳酸钠或者碳酸氢钠。In a preferred embodiment of the present invention, the shower device or the drip device is provided with dilute hydrochloric acid, dilute nitric acid, dilute sulfuric acid, sodium hydroxide, potassium hydroxide, sodium carbonate or sodium hydrogencarbonate.
在本发明一个较佳实施例中，所述第二固体处理装置内设置有过滤装置，所述过滤装置的孔径小于0.1mm。In a preferred embodiment of the present invention, the second solid processing apparatus is provided with a filtering device having a pore diameter of less than 0.1 mm.
在本发明一个较佳实施例中，所述第一液体处理装置内设置有石炭网，所述石炭网的厚度大于2mm。In a preferred embodiment of the present invention, the first liquid processing apparatus is provided with a carbonaceous mesh having a thickness greater than 2 mm.
在本发明一个较佳实施例中，所述第二液体处理装置内设置有离子交换膜。In a preferred embodiment of the invention, an ion exchange membrane is disposed within the second liquid processing apparatus.
在本发明一个较佳实施例中，所述收集装置为球形。In a preferred embodiment of the invention, the collection device is spherical.
本发明的有益效果是：本发明用于化学废水的回收及多级处理玻璃装置通过固液分别多级处理净化，针对性强、净化彻底、处理方便、效率高、安全实用，在用于化学废水的回收及多级处理玻璃装置的普
及上有着广泛的市场前景。The invention has the beneficial effects that the invention is used for the recovery of chemical wastewater and the multi-stage treatment glass device is purified by multi-stage treatment by solid-liquid, and has strong pertinence, thorough purification, convenient treatment, high efficiency, safety and practicability, and is used in chemistry. Wastewater recovery and multi-stage treatment of glass equipment
There is a broad market prospect.
为了更清楚地说明本发明实施例中的技术方案，下面将对实施例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一些实施例，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，还可以根据这些附图获得其它的附图，其中：In order to more clearly illustrate the technical solutions in the embodiments of the present invention, the drawings used in the description of the embodiments will be briefly described below. It is obvious that the drawings in the following description are only some embodiments of the present invention. For those skilled in the art, other drawings can be obtained according to these drawings without any creative work, wherein:
图1是本发明的用于化学废水的回收及多级处理玻璃装置一较佳实施例的结构示意图。BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a schematic view showing the structure of a preferred embodiment of a multi-stage processing glass apparatus for recovering chemical waste water according to the present invention.
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，所描述的实施例仅是本发明的一部分实施例，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它实施例，都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below. It is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments obtained by a person of ordinary skill in the art based on the embodiments of the present invention without creative efforts are within the scope of the present invention.
请参阅图1，本发明实施例包括：Referring to FIG. 1, an embodiment of the present invention includes:
一种用于化学废水的回收及多级处理玻璃装置，包括：若干回收装置2、静置装置1、第一固体处理装置3、第二固体处理装置4、第一液体处理装置5、第二液体处理装置6和收集装置7。A recycling and multi-stage processing glass device for chemical wastewater, comprising: a plurality of recovery devices 2, a standing device 1, a first solid processing device 3, a second solid processing device 4, a first liquid processing device 5, and a second Liquid treatment device 6 and collection device 7.
所述若干回收装置2分别连通连接所述静置装置1，让废水在所述静置装置1中静置一段时间实现分层，所述第一固体处理装置3通过第一二通阀连通连接所述静置装置1的底部，当需要处理底部的沉降废水时，打开所述第一二通阀，所述第二固体处理装置4连通连接
所述第一固体处理装置3的输出端，沉降的废水分别经由所述第一固体处理装置3、第二固体处理装置4进行净化处理，所述第一液体处理装置5通过第二二通阀连通连接所述静置装置1的上部的侧面，当需要处理上层废水时，打开所述第二二通阀，所述第二液体处理装置6连通连接所述第一液体处理装置5的输出端，上层废水分别经由所述第一液体处理装置5、第二液体处理装置6进行净化处理，所述第二固体处理装置4与所述第二液体处理装置6的输出端分别连通连接所述收集装置7，最终处理后的水汇聚到所述收集装置7等待进一步的回收处理。The plurality of recovery devices 2 are respectively connected to the stationary device 1 to allow the wastewater to stand in the stationary device 1 for a period of time to achieve stratification, and the first solid processing device 3 is connected through the first two-way valve. The bottom of the stationary device 1 opens the first two-way valve when the sedimentation wastewater at the bottom needs to be treated, and the second solid processing device 4 is connected
The output end of the first solid processing device 3, the settled wastewater is purified by the first solid processing device 3 and the second solid processing device 4, respectively, and the first liquid processing device 5 passes through the second two-way valve Connecting the side of the upper portion of the stationary device 1 to open the second two-way valve when the upper layer wastewater needs to be treated, and the second liquid processing device 6 is connected to the output end of the first liquid processing device 5 The upper layer wastewater is subjected to purification treatment via the first liquid processing device 5 and the second liquid processing device 6, respectively, and the second solid processing device 4 and the output end of the second liquid processing device 6 are respectively connected to the collection. Device 7, the final treated water is concentrated to the collection device 7 for further recovery processing.
优选地，所述若干回收装置2的开口口径向远离所述静置装置1的方向依次增大，方便倾倒、防止漏洒。Preferably, the opening ports of the plurality of recovery devices 2 are sequentially increased radially away from the direction of the stationary device 1 to facilitate pouring and preventing leakage.
优选地，所述静置装置1的横截面形状为圆形。Preferably, the standing device 1 has a circular cross section shape.
优选地，所述静置装置1的横截面直径由所述静置装置1的中间向两端的方向依次增大，有利于废水分层。Preferably, the cross-sectional diameter of the stationary device 1 is sequentially increased from the middle to the both ends of the stationary device 1 to facilitate stratification of the wastewater.
优选地，所述第一固体处理装置3的顶部设置有喷淋装置或者滴液装置。Preferably, the top of the first solid processing device 3 is provided with a shower device or a drip device.
优选地，所述喷淋装置或者所述滴液装置内放置稀盐酸、稀硝酸、稀硫酸、氢氧化钠、氢氧化钾、碳酸钠或者碳酸氢钠，通过向沉降废水喷淋或者滴洒选择的酸性液体或者碱性液体，利用化学反应来消除难溶于水的固体沉降物。Preferably, the shower device or the drip device is provided with dilute hydrochloric acid, dilute nitric acid, dilute sulfuric acid, sodium hydroxide, potassium hydroxide, sodium carbonate or sodium hydrogencarbonate, and is selected by spraying or dripping the sedimentation wastewater. An acidic liquid or an alkaline liquid that utilizes a chemical reaction to remove solid deposits that are poorly soluble in water.
优选地，所述第二固体处理装置4内设置有过滤装置401，所述过滤装置401的孔径小于0.1mm，利用过滤装置401对固体残渣进行
过滤，进一步分离固体。Preferably, the second solid processing device 4 is provided with a filtering device 401 having a pore diameter of less than 0.1 mm, and the solid residue is performed by the filtering device 401.
Filter to further separate the solids.
优选地，所述第一液体处理装置5内设置有石炭网501，所述石炭网501的厚度大于2mm，石炭有利于吸附异物。Preferably, the first liquid processing device 5 is provided with a carbonaceous mesh 501 having a thickness greater than 2 mm, and the charcoal is favorable for adsorbing foreign matter.
优选地，所述第二液体处理装置6内设置有离子交换膜601，所述离子交换膜601用于分离溶于水的离子。Preferably, the second liquid processing device 6 is provided with an ion exchange membrane 601 for separating ions dissolved in water.
优选地，所述收集装置7为球形。Preferably, the collection device 7 is spherical.
本发明用于化学废水的回收及多级处理玻璃装置的有益效果是：The beneficial effects of the invention for the recovery of chemical wastewater and the multi-stage treatment of the glass device are:
通过固液分别多级处理净化，针对性强、净化彻底、处理方便、效率高、安全实用。It is multi-staged and purified by solid-liquid treatment, with strong pertinence, thorough purification, convenient treatment, high efficiency, safety and practicality.
以上所述仅为本发明的实施例，并非因此限制本发明的专利范围，凡是利用本发明说明书内容所作的等效结构或等效流程变换，或直接或间接运用在其它相关的技术领域，均同理包括在本发明的专利保护范围内。
The above is only the embodiment of the present invention, and thus does not limit the scope of the patent of the present invention. Any equivalent structure or equivalent process transformation made by using the contents of the specification of the present invention, or directly or indirectly applied to other related technical fields, The same is included in the scope of patent protection of the present invention.
Claims (10)
- 一种用于化学废水的回收及多级处理玻璃装置，其特征在于，包括：若干回收装置、静置装置、第一固体处理装置、第二固体处理装置、第一液体处理装置、第二液体处理装置和收集装置，所述若干回收装置分别连通连接所述静置装置，所述第一固体处理装置通过第一二通阀连通连接所述静置装置的底部，所述第二固体处理装置连通连接所述第一固体处理装置的输出端，所述第一液体处理装置通过第二二通阀连通连接所述静置装置的上部的侧面，所述第二液体处理装置连通连接所述第一液体处理装置的输出端，所述第二固体处理装置与所述第二液体处理装置的输出端分别连通连接所述收集装置。A recycling and multi-stage processing glass device for chemical wastewater, comprising: a plurality of recovery devices, a standing device, a first solid processing device, a second solid processing device, a first liquid processing device, and a second liquid a processing device and a collecting device, wherein the plurality of recycling devices are respectively connected to the stationary device, and the first solid processing device is connected to the bottom of the stationary device through a first two-way valve, the second solid processing device Connected to an output end of the first solid processing device, the first liquid processing device is connected to a side surface of an upper portion of the stationary device through a second two-way valve, and the second liquid processing device is connected to the first An output end of a liquid processing device, the second solid processing device and the output end of the second liquid processing device are respectively connected to the collecting device.
- 根据权利要求1所述的用于化学废水的回收及多级处理玻璃装置，其特征在于，所述若干回收装置的开口口径向远离所述静置装置的方向依次增大。The apparatus for recovering and multi-stage processing of chemical waste water according to claim 1, wherein the opening ports of the plurality of recovery devices are sequentially increased radially away from the direction of the stationary device.
- 根据权利要求1所述的用于化学废水的回收及多级处理玻璃装置，其特征在于，所述静置装置的横截面形状为圆形。The apparatus for recycling and multi-stage processing of chemical waste water according to claim 1, wherein the standing device has a circular cross section.
- 根据权利要求3所述的用于化学废水的回收及多级处理玻璃装置，其特征在于，所述静置装置的横截面直径由所述静置装置的中间向两端的方向依次增大。The apparatus for recovering and multi-stage processing of chemical waste water according to claim 3, wherein a cross-sectional diameter of said standing means is sequentially increased from a middle to a both ends of said standing means.
- 根据权利要求1所述的用于化学废水的回收及多级处理玻璃装置，其特征在于，所述第一固体处理装置的顶部设置有喷淋装置或者滴液装置。The apparatus for recycling and multi-stage processing of chemical waste water according to claim 1, wherein a top of the first solid-state treatment device is provided with a shower device or a drip device.
- 根据权利要求5所述的用于化学废水的回收及多级处理玻璃装置， 其特征在于，所述喷淋装置或者所述滴液装置内放置稀盐酸、稀硝酸、稀硫酸、氢氧化钠、氢氧化钾、碳酸钠或者碳酸氢钠。A recycling and multi-stage processing glass apparatus for chemical wastewater according to claim 5, It is characterized in that the shower device or the drip device is provided with dilute hydrochloric acid, dilute nitric acid, dilute sulfuric acid, sodium hydroxide, potassium hydroxide, sodium carbonate or sodium hydrogencarbonate.
- 根据权利要求1所述的用于化学废水的回收及多级处理玻璃装置，其特征在于，所述第二固体处理装置内设置有过滤装置，所述过滤装置的孔径小于0.1mm。The apparatus for recycling and multi-stage processing of chemical waste water according to claim 1, wherein a filter device is disposed in the second solid-state treatment device, and the filter device has a pore diameter of less than 0.1 mm.
- 根据权利要求1所述的用于化学废水的回收及多级处理玻璃装置，其特征在于，所述第一液体处理装置内设置有石炭网，所述石炭网的厚度大于2mm。The apparatus for recycling and multi-stage processing of chemical waste water according to claim 1, wherein a carbonaceous net is disposed in the first liquid processing apparatus, and the thickness of the carbonaceous net is greater than 2 mm.
- 根据权利要求1所述的用于化学废水的回收及多级处理玻璃装置，其特征在于，所述第二液体处理装置内设置有离子交换膜。The apparatus for recovering and treating a chemical waste water according to claim 1, wherein the second liquid processing apparatus is provided with an ion exchange membrane.
- 根据权利要求1所述的用于化学废水的回收及多级处理玻璃装置，其特征在于，所述收集装置为球形。 A recycling and multi-stage processing glass apparatus for chemical wastewater according to claim 1, wherein said collecting means is spherical.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620144491.1U CN205398270U (en) | 2016-02-26 | 2016-02-26 | A retrieve and multilevel processing glass device for chemical waste water |
| CN201620144491.1 | 2016-02-26 |
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| Publication Number | Publication Date |
|---|---|
| WO2017143806A1 true WO2017143806A1 (en) | 2017-08-31 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/CN2016/105689 WO2017143806A1 (en) | 2016-02-26 | 2016-11-14 | Glass device for recovering and multilevel processing chemical waste water |
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| Country | Link |
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| CN (1) | CN205398270U (en) |
| WO (1) | WO2017143806A1 (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113666519A (en) * | 2021-08-06 | 2021-11-19 | 连云港原舜光伏材料有限公司 | High-purity quartz sand water mill wastewater recovery treatment device and treatment method thereof |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN205398270U (en) * | 2016-02-26 | 2016-07-27 | 盐城市华鸥实业有限公司 | A retrieve and multilevel processing glass device for chemical waste water |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1144776A (en) * | 1995-03-27 | 1997-03-12 | 国际废水处理集团 | Apparatus and method for treatment of dye mill liquors |
| EP0985657A1 (en) * | 1998-08-11 | 2000-03-15 | BP Chemicals Limited | Improved process for the production of vinyl acetate |
| CN2797348Y (en) * | 2005-04-05 | 2006-07-19 | 张今心 | Purifier for waste liquid from chemical lab of middle school |
| EP2246767A1 (en) * | 2006-01-27 | 2010-11-03 | Millipore Corporation | A polishing cartridge for final purification of water for distribution to a point of use |
| CN203007063U (en) * | 2012-12-05 | 2013-06-19 | 西南科技大学 | Comprehensive wastewater treatment device of inorganic laboratory |
| CN103466833A (en) * | 2013-09-10 | 2013-12-25 | 西北稀有金属材料研究院 | Treatment method of beryllium-containing sewage |
| CN205398270U (en) * | 2016-02-26 | 2016-07-27 | 盐城市华鸥实业有限公司 | A retrieve and multilevel processing glass device for chemical waste water |
-
2016
- 2016-02-26 CN CN201620144491.1U patent/CN205398270U/en not_active Expired - Fee Related
- 2016-11-14 WO PCT/CN2016/105689 patent/WO2017143806A1/en active Application Filing
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1144776A (en) * | 1995-03-27 | 1997-03-12 | 国际废水处理集团 | Apparatus and method for treatment of dye mill liquors |
| EP0985657A1 (en) * | 1998-08-11 | 2000-03-15 | BP Chemicals Limited | Improved process for the production of vinyl acetate |
| CN2797348Y (en) * | 2005-04-05 | 2006-07-19 | 张今心 | Purifier for waste liquid from chemical lab of middle school |
| EP2246767A1 (en) * | 2006-01-27 | 2010-11-03 | Millipore Corporation | A polishing cartridge for final purification of water for distribution to a point of use |
| CN203007063U (en) * | 2012-12-05 | 2013-06-19 | 西南科技大学 | Comprehensive wastewater treatment device of inorganic laboratory |
| CN103466833A (en) * | 2013-09-10 | 2013-12-25 | 西北稀有金属材料研究院 | Treatment method of beryllium-containing sewage |
| CN205398270U (en) * | 2016-02-26 | 2016-07-27 | 盐城市华鸥实业有限公司 | A retrieve and multilevel processing glass device for chemical waste water |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113666519A (en) * | 2021-08-06 | 2021-11-19 | 连云港原舜光伏材料有限公司 | High-purity quartz sand water mill wastewater recovery treatment device and treatment method thereof |
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| CN205398270U (en) | 2016-07-27 |
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