CN217438309U - Hydrogen peroxide synthesizer and medical effluent disposal system - Google Patents
Hydrogen peroxide synthesizer and medical effluent disposal system Download PDFInfo
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- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 title claims abstract description 82
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- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 21
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
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Abstract
Description
技术领域technical field
本实用新型涉及一种过氧化氢合成装置及一种医用废水处理系统,属于环境科学技术领域。The utility model relates to a hydrogen peroxide synthesis device and a medical waste water treatment system, belonging to the technical field of environmental science.
背景技术Background technique
医用废水主要是过期药品、医用器具上残留的抗生素溶注水体形成的。而常用的降解医用废水中抗生素的主要方法是芬顿氧化法(Fenton)。Medical wastewater is mainly formed by the dissolution of antibiotics remaining on expired medicines and medical equipment into water bodies. The main method commonly used to degrade antibiotics in medical wastewater is Fenton oxidation.
芬顿氧化法是最常用的处理废水技术,具有反应速度快、反应条件温和、反应彻底等特点。芬顿氧化法通常是先向废水中添加二价铁盐(Fe2+),然后再添加过氧化氢(H2O2),Fe2+作为催化剂将H2O2还原为·OH和H2O,由于·OH的氧化电位仅次于氟的氧化电位,因此·OH能够氧化分解废水中的有机污染物,在氧化反应过程中,氧化电位可高达2.8 V,当芬顿反应结束后,继续向废水中添加碱试剂,能够使金属离子沉淀。Fenton oxidation is the most commonly used wastewater treatment technology, which has the characteristics of fast reaction speed, mild reaction conditions and thorough reaction. The Fenton oxidation method is usually to add divalent iron salt (Fe 2+ ) to the wastewater first, then add hydrogen peroxide (H 2 O 2 ), and Fe 2+ acts as a catalyst to reduce H 2 O 2 to OH and H 2 O. Since the oxidation potential of OH is second only to that of fluorine, OH can oxidize and decompose organic pollutants in wastewater. During the oxidation reaction, the oxidation potential can be as high as 2.8 V. After the Fenton reaction, the Continuing to add alkaline reagents to the wastewater can precipitate metal ions.
基于此,本申请提供一种过氧化氢合成装置及一种医用废水处理系统。Based on this, the present application provides a hydrogen peroxide synthesis device and a medical wastewater treatment system.
实用新型内容Utility model content
本实用新型的目的在于克服现有技术中的不足,提供一种过氧化氢合成装置及一种医用废水处理系统,能够绿色合成过氧化氢,并安全有效地处理医用废水。The purpose of the utility model is to overcome the deficiencies in the prior art, and to provide a hydrogen peroxide synthesis device and a medical waste water treatment system, which can synthesize hydrogen peroxide in a green way and safely and effectively treat the medical waste water.
为达到上述目的,本实用新型是采用下述技术方案实现的:In order to achieve the above object, the utility model adopts the following technical solutions to realize:
一方面,本实用新型提供一种过氧化氢合成装置,包括太阳能电池板、整流器、蓄电池组、阳极单元、合成单元、阴极单元以及储存单元;In one aspect, the present invention provides a hydrogen peroxide synthesis device, comprising a solar cell panel, a rectifier, a battery pack, an anode unit, a synthesis unit, a cathode unit and a storage unit;
所述太阳能电池板输出端连接整流器输入端,整流器输出端连接蓄电池组输入端,蓄电池组正极连接阳极单元,蓄电池组负极连接阴极单元;The output end of the solar panel is connected to the input end of the rectifier, the output end of the rectifier is connected to the input end of the battery pack, the positive pole of the battery pack is connected to the anode unit, and the negative pole of the battery pack is connected to the cathode unit;
所述合成单元上开设有出口,出口管路连接储存单元;The synthesis unit is provided with an outlet, and the outlet pipeline is connected to the storage unit;
所述合成单元内设有固体电解质,固体电解质一端连接阳极单元,固体电解质另一端连接阴极单元;The synthesis unit is provided with a solid electrolyte, one end of the solid electrolyte is connected to the anode unit, and the other end of the solid electrolyte is connected to the cathode unit;
进一步地,所述阳极单元包括顺次设置的第一扩散层、第一胶质层以及阳离子交换膜;Further, the anode unit includes a first diffusion layer, a first colloid layer and a cation exchange membrane arranged in sequence;
所述第一胶质层连接蓄电池组正极;The first colloidal layer is connected to the positive electrode of the battery pack;
所述阳离子交换膜连接合成单元。The cation exchange membrane connects the synthesis unit.
进一步地,所述阴极单元包括顺次设置的第二扩散层、第二胶质层以及阴离子交换膜;Further, the cathode unit includes a second diffusion layer, a second colloid layer and an anion exchange membrane arranged in sequence;
所述第二胶质层连接蓄电池组正极;The second glue layer is connected to the positive electrode of the battery pack;
所述阴离子交换膜连接合成单元。The anion exchange membrane connects the synthesis units.
另一方面,本实用新型提供一种医用废水处理系统,包括上述的过氧化氢合成装置以及顺次连接的调节池、水解酸化池、氧化池、沉淀区和消毒池;On the other hand, the present utility model provides a medical waste water treatment system, comprising the above-mentioned hydrogen peroxide synthesis device and a regulating tank, a hydrolysis acidification tank, an oxidation tank, a sedimentation area and a disinfection tank connected in sequence;
所述消毒池输入端连接过氧化氢合成装置的储存单元输出端。The input end of the disinfection tank is connected to the output end of the storage unit of the hydrogen peroxide synthesis device.
进一步地,所述的医用废水处理系统包括供氧风机;Further, the medical wastewater treatment system includes an oxygen supply fan;
所述供氧风机出风口分别连接调节池和氧化池。The air outlet of the oxygen supply fan is respectively connected to the adjustment tank and the oxidation tank.
进一步地,所述的医用废水处理系统包括集泥区;Further, the medical wastewater treatment system includes a mud collecting area;
所述集泥区输入端分别连接调节池、沉淀区和水解酸化池。The input ends of the mud collecting area are respectively connected with the regulating tank, the sedimentation area and the hydrolysis and acidification tank.
进一步地,所述氧化池内挂设有生物膜。Further, a biofilm is hung in the oxidation tank.
进一步地,所述调节池内设有PH值调节装置和缓冲剂添加装置。Further, a pH value adjusting device and a buffer adding device are arranged in the adjusting tank.
进一步地,所述沉淀区包括多个平行设置的斜板或斜管。Further, the precipitation zone includes a plurality of inclined plates or inclined tubes arranged in parallel.
与现有技术相比,本实用新型所达到的有益效果:Compared with the prior art, the beneficial effects achieved by the present utility model:
本实用新型利用固体电解质合成过氧化氢,避免使用有机溶液,不仅减少了提纯和净化成本,还缩短了合成过氧化氢的步骤,提高了效率。本实用新型利用太阳能发电合成过氧化氢,能够节约能源,实现清洁生产;The utility model utilizes the solid electrolyte to synthesize hydrogen peroxide, avoids the use of organic solutions, not only reduces the cost of purification and purification, but also shortens the steps of synthesizing hydrogen peroxide and improves the efficiency. The utility model utilizes solar energy to generate electricity to synthesize hydrogen peroxide, which can save energy and realize clean production;
本实用新型利用过氧化氢合成装置获得过氧化氢水溶液,现产现用,降低了过氧化氢运输中的危险性,能够安全有效地处理医用废水。The utility model utilizes a hydrogen peroxide synthesis device to obtain an aqueous hydrogen peroxide solution, which is currently produced and used, reduces the danger in the transportation of hydrogen peroxide, and can safely and effectively treat medical waste water.
附图说明Description of drawings
图1所示为本实用新型医用废水处理系统的一种实施例结构示意图;FIG. 1 is a schematic structural diagram of an embodiment of the medical wastewater treatment system of the present invention;
图2所示为本实用新型过氧化氢合成装置的一种实施例结构示意图;Fig. 2 shows a kind of embodiment structural representation of the hydrogen peroxide synthesis device of the present utility model;
图3所示为本实用新型过氧化氢合成装置的一种实施例结构示意图;Fig. 3 shows a kind of embodiment structural representation of the hydrogen peroxide synthesis device of the present utility model;
图中:1、太阳能电池板,2、整流器,3蓄电池组,4、合成模组,5、储存单元,6、调节池,7、水解酸化池,8、氧化池,9、沉淀区,10、消毒池,11、集泥区,12、供氧风机,41、阳极单元,42、阴极单元,43、合成单元,411、第一进水口,412、排水口,413、第一出氧口,414、第一扩散层,415、第一胶质层,416、阳离子交换膜,421、第二进水口,422、进氧口,423、第二出氧口,424、第二扩散层,425、第二胶质层,426、阴离子交换膜,431、出口,432、固体电解质。In the picture: 1. Solar panel, 2. Rectifier, 3. Battery pack, 4. Synthesis module, 5. Storage unit, 6. Regulating tank, 7. Hydrolysis and acidification tank, 8. Oxidation tank, 9. Precipitation area, 10 , disinfection tank, 11, sludge collection area, 12, oxygen supply fan, 41, anode unit, 42, cathode unit, 43, synthesis unit, 411, first water inlet, 412, water outlet, 413, first oxygen outlet , 414, the first diffusion layer, 415, the first colloidal layer, 416, the cation exchange membrane, 421, the second water inlet, 422, the oxygen inlet, 423, the second oxygen outlet, 424, the second diffusion layer, 425, second colloidal layer, 426, anion exchange membrane, 431, outlet, 432, solid electrolyte.
具体实施方式Detailed ways
下面结合附图对本实用新型作进一步描述。以下实施例仅用于更加清楚地说明本实用新型的技术方案,而不能以此来限制本实用新型的保护范围。The present utility model will be further described below in conjunction with the accompanying drawings. The following examples are only used to illustrate the technical solutions of the present invention more clearly, and cannot be used to limit the protection scope of the present invention.
在本实用新型的描述中,需要理解的是,术语“中心”、“纵向”、“横向”、“上”、“下”、“前”、“后”、“左”、“右”、“竖直”、“水平”、“顶”、 “底”、“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本实用新型和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本实用新型的限制。此外,术语“第一”、“第二”等仅用于描述目的,而不能理解为指示或暗示相对重要性或者隐含指明所指示的技术特征的数量。由此,限定有“第一”、“第二”等的特征可以明示或者隐含地包括一个或者更多个该特征。在本实用新型的描述中,除非另有说明,“多个”的含义是两个或两个以上。In the description of the present invention, it should be understood that the terms "center", "longitudinal", "horizontal", "upper", "lower", "front", "rear", "left", "right", The orientations or positional relationships indicated by "vertical", "horizontal", "top", "bottom", "inside", "outside", etc. are based on the orientations or positional relationships shown in the accompanying drawings, and are only for the convenience of describing the present invention The novel and simplified description does not indicate or imply that the device or element referred to must have a particular orientation, be constructed and operate in a particular orientation, and therefore should not be construed as limiting the invention. In addition, the terms "first", "second", etc. are used for descriptive purposes only, and should not be construed as indicating or implying relative importance or implying the number of indicated technical features. Thus, a feature defined as "first", "second", etc., may expressly or implicitly include one or more of that feature. In the description of the present invention, unless otherwise specified, "plurality" means two or more.
在本实用新型的描述中,需要说明的是,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通。对于本领域的普通技术人员而言,可以通过具体情况理解上述术语在本实用新型中的具体含义。In the description of the present invention, it should be noted that, unless otherwise expressly specified and limited, the terms "installed", "connected" and "connected" should be understood in a broad sense, for example, it may be a fixed connection or a connectable connection. Detachable connection, or integral connection; may be mechanical connection or electrical connection; may be direct connection or indirect connection through an intermediate medium, or internal communication between two components. For those of ordinary skill in the art, the specific meanings of the above terms in the present invention can be understood through specific situations.
实施例1Example 1
过氧化氢是一种适用于多种工业应用的原料或产品,其水溶液具有强氧化性适用于医用、食品和环境消毒,本实施例提供一种过氧化氢合成装置。Hydrogen peroxide is a raw material or product suitable for various industrial applications, and its aqueous solution has strong oxidizing properties and is suitable for medical, food and environmental disinfection. This embodiment provides a hydrogen peroxide synthesis device.
参考图2,过氧化氢合成装置包括太阳能电池板1、整流器2、蓄电池组3、合成模组4以及储存单元5。Referring to FIG. 2 , the hydrogen peroxide synthesis device includes a solar cell panel 1 , a rectifier 2 , a
参考图3,合成模组4包括顺次设置的阳极单元41、合成单元43以及阴极单元42。Referring to FIG. 3 , the synthesis module 4 includes an
本实施例实际应用时,太阳能电池板输出端连接整流器输入端,整流器输出端连接蓄电池组输入端,蓄电池组正极连接阳极单元41,蓄电池组负极连接阴极单元42。In practical application of this embodiment, the output end of the solar panel is connected to the input end of the rectifier, the output end of the rectifier is connected to the input end of the battery pack, the positive pole of the battery pack is connected to the
参考图2,阳极单元41上开设有第一进水口411、第一出氧口413、排水口412。Referring to FIG. 2 , the
应用中,第一进水口411外接供水装置,以获得去离子水,提高产率;第一出氧口413外接废气收集装置;排水口412外接废液收集装置。In application, the
阳极单元发生水解:2H2O–4e-→4H++O2(酸性);The anode unit undergoes hydrolysis: 2H 2 O–4e - →4H + +O 2 (acidic);
参考图2,阴极单元42上开设有进氧口422、第二出氧口423、第二进水口421。Referring to FIG. 2 , the
应用中,进氧口422外接供氧装置;第二出氧口423外接废气收集装置;第二进水口421外接供水装置。In application, the
阴极单元发生水解:O2+H2O+2e-→HO2 -+OH-;The cathode unit undergoes hydrolysis: O 2 +H 2 O+2e - →HO 2 - +OH - ;
参考图3,合成单元43内设有固体电解质432,固体电解质432一端连接阳极单元41,固体电解质432另一端连接阴极单元42。Referring to FIG. 3 , the
应用中,固体电解质432包括多层固体电解质432,各层固体电解质432为多孔苯乙烯-二乙烯基苯磺化共聚物。In application, the
合成单元发生过氧化氢合成反应:HO2 -+H+→H2O2。The synthesis unit takes place in the hydrogen peroxide synthesis reaction: HO 2 - +H + →H 2 O 2 .
本实施例实际应用时,过氧化氢生产率高达3.4 mmol/cm2/h,过氧化氢水溶液浓度高达20%。In the practical application of this embodiment, the hydrogen peroxide productivity is as high as 3.4 mmol/cm 2 /h, and the concentration of the hydrogen peroxide aqueous solution is as high as 20%.
参考图2,合成单元43上开设有出口431,出口431管路连接储存单元5,储存单元5用于储存过氧化氢。Referring to FIG. 2 , the
本实用新型利用固体电解质合成过氧化氢,避免使用有机溶液,不仅减少了提纯和净化成本,还缩短了合成过氧化氢的步骤,提高了效率。本实用新型利用太阳能发电合成过氧化氢,能够节约能源,实现清洁生产。The utility model utilizes the solid electrolyte to synthesize hydrogen peroxide, avoids the use of organic solutions, not only reduces the cost of purification and purification, but also shortens the steps of synthesizing hydrogen peroxide and improves the efficiency. The utility model utilizes solar energy to generate electricity to synthesize hydrogen peroxide, which can save energy and realize clean production.
实施例2Example 2
在实施例1的基础上,本实施例详细介绍了阳极单元和阴极单元。On the basis of Embodiment 1, this embodiment introduces the anode unit and the cathode unit in detail.
参考图3,阳极单元41包括顺次设置的第一扩散层414、第一胶质层415以及阳离子交换膜416。Referring to FIG. 3 , the
应用中,第一胶质层415连接蓄电池组正极;阳离子交换膜416连接合成单元43的固体电解质432。In application, the first
参考图3,阴极单元42包括顺次设置的第二扩散层424、第二胶质层425以及阴离子交换膜426;Referring to FIG. 3 , the
应用中,第二胶质层425连接蓄电池组正极;阴离子交换膜426连接合成单元43的固体电解质432。In application, the second
本实用新型阳离子交换膜能够筛滤H+,阴离子交换膜能够筛滤HO2 -,固体电解质直接利用阳离子交换膜和阴离子交换膜筛滤后的H+和HO2 -合成H2O2,避免使用有机溶液作为溶剂减少了提纯和净化成本。The cation exchange membrane of the utility model can filter H + , the anion exchange membrane can filter HO 2 - , and the solid electrolyte directly utilizes the H + and HO 2 - filtered by the cation exchange membrane and the anion exchange membrane to synthesize H 2 O 2 , avoiding the need for The use of organic solutions as solvents reduces purification and purification costs.
实施例3Example 3
由于医用废水中含有大量病菌、病毒和其他有毒有害物质以及抗生素等,本实施例提供一种医用废水处理系统。Since medical wastewater contains a large number of germs, viruses, other toxic and harmful substances, antibiotics, etc., this embodiment provides a medical wastewater treatment system.
参考图1,医用废水处理系统包括实施例1或2记载的过氧化氢合成装置以及顺次连接的调节池6、水解酸化池7、氧化池8、沉淀区9和消毒池10。1 , the medical wastewater treatment system includes the hydrogen peroxide synthesis device described in Example 1 or 2, and a conditioning tank 6 , a hydrolysis and acidification tank 7 , an oxidation tank 8 , a sedimentation zone 9 and a
应用中,医院综合污水经化粪池预处理后获得医用废水,医用废水经格栅井沉沙,即去除大颗粒悬浮物和纤维杂质后,进入调节池(6)。In the application, the hospital comprehensive sewage is pretreated by the septic tank to obtain medical waste water, and the medical waste water is sanded through the grid well, that is, after removing large particles of suspended solids and fibrous impurities, it enters the regulating tank (6).
参考图1,调节池(6)输出端连接水解酸化池(7)输入端,水解酸化池(7)连接氧化池(8),氧化池(8)输出端连接沉淀区(9)输入端,沉淀区(9)输入端连接消毒池输入端。Referring to Figure 1, the output end of the adjustment tank (6) is connected to the input end of the hydrolysis and acidification tank (7), the hydrolysis acidification tank (7) is connected to the oxidation tank (8), and the output end of the oxidation tank (8) is connected to the input end of the precipitation zone (9). The input end of the sedimentation zone (9) is connected to the input end of the disinfection tank.
应用中,调节池(6)内设有提升水泵和混凝沉淀单元,医用废水经提升后进入混凝沉淀单元进行混凝沉淀,并经混凝沉淀单元输出进入水解酸化池(7),水解酸化池(7)和氧化池(8)之间设置有内循环装置,即进入氧化池(8)的医用废水通过内循环装置进入水解酸化池(7),以提高医用废水的酸化氧化程度。In application, the regulating tank (6) is provided with a lifting pump and a coagulation and sedimentation unit. The medical wastewater is lifted into the coagulation and sedimentation unit for coagulation and sedimentation, and is output into the hydrolysis and acidification tank (7) through the coagulation and sedimentation unit for hydrolysis. An internal circulation device is arranged between the acidification tank (7) and the oxidation tank (8), that is, the medical wastewater entering the oxidation tank (8) enters the hydrolysis and acidification tank (7) through the internal circulation device to improve the acidification and oxidation degree of the medical wastewater.
参考图1,消毒池输入端连接过氧化氢合成装置的储存单元输出端。Referring to Figure 1, the input end of the disinfection tank is connected to the output end of the storage unit of the hydrogen peroxide synthesis device.
参考图2,储存单元输出端与消毒池输入端之间设有计量加药泵,用以调控消毒池中过氧化氢的浓度。Referring to FIG. 2 , a metering dosing pump is arranged between the output end of the storage unit and the input end of the disinfection tank to regulate the concentration of hydrogen peroxide in the disinfection tank.
本实用新型通过过氧化氢合成装置获得浓度为20%的过氧化氢水溶液,现产现用,降低了过氧化氢运输中的危险性,能够有效处理医用废水。The utility model obtains a hydrogen peroxide aqueous solution with a concentration of 20% through a hydrogen peroxide synthesis device, which is currently produced and used, reduces the danger in the transportation of hydrogen peroxide, and can effectively treat medical waste water.
实施例4Example 4
在实施例3的基础上,本实施例详细介绍了医用废水处理系统的调节池6、水解酸化池7、氧化池8、沉淀区9、消毒池10、供氧风机12和集泥区11。On the basis of Example 3, this example introduces in detail the conditioning tank 6, the hydrolysis acidification tank 7, the oxidation tank 8, the sedimentation area 9, the
本实施例的医用废水处理系统还包括供氧风机12和集泥区11。其中,集泥区11输入端分别连接调节池6、沉淀区9和水解酸化池7,集泥区11输出端连接污泥外运装置,以保持系统的清洁度和医用废水的处理能力。此外,供氧风机12出风口分别连接调节池6和氧化池8。The medical wastewater treatment system of this embodiment further includes an oxygen supply fan 12 and a mud collecting area 11 . Among them, the input end of the sludge collecting area 11 is connected to the regulating tank 6, the sedimentation area 9 and the hydrolysis and acidification tank 7 respectively, and the output end of the sludge collecting area 11 is connected to the sludge outgoing device to maintain the cleanliness of the system and the treatment capacity of medical wastewater. In addition, the air outlet of the oxygen supply fan 12 is connected to the adjustment tank 6 and the oxidation tank 8 respectively.
(1)调节池(1) Adjustment pool
调节池6为钢筋混凝土结构,内设有PH值调节装置和缓冲剂添加装置,用于调节医用废水的酸性环境和稳定性。The regulating tank 6 is of reinforced concrete structure, and is equipped with a pH value regulating device and a buffer adding device, which are used to regulate the acid environment and stability of medical wastewater.
(2)水解酸化池(2) Hydrolysis and acidification tank
水解酸化池7为碳钢防腐结构。主要目的是为了将原有废水中的非溶解性有机物转变为溶解性有机物,将难生物降解的有机物转变为易生物降解的有机物,提高废水的可生化性,以便于后续的氧化处理。The hydrolysis and acidification tank 7 is a carbon steel anti-corrosion structure. The main purpose is to convert the insoluble organic matter in the original wastewater into soluble organic matter, convert the refractory organic matter into easily biodegradable organic matter, and improve the biodegradability of the wastewater to facilitate subsequent oxidation treatment.
(3)氧化池(3) Oxidation pool
氧化池8内挂设有生物膜,生物膜上附有菌株。A biofilm is hung in the oxidation tank 8, and bacterial strains are attached to the biofilm.
生物膜的比表面积大,池内的充氧条件好,空气流动性好,使得医用废水与生物膜之间产生较大的相对速度,加快了细菌表面的介质更新,增强了传质效果,加快生物代谢速度,缩短了处理时间。The specific surface area of the biofilm is large, the oxygenation conditions in the pool are good, and the air flow is good, which makes the medical wastewater and the biofilm produce a relatively large relative speed, which accelerates the renewal of the medium on the surface of the bacteria, enhances the mass transfer effect, and accelerates the biological process. Metabolic speed, shortened processing time.
(4)沉淀区(4) Precipitation area
沉淀区9包括多个平行设置的斜板或斜管,用于将进入沉淀区9的医用废水水流分隔成薄层,以提高沉淀效率。The precipitation zone 9 includes a plurality of inclined plates or inclined tubes arranged in parallel, which are used to separate the medical waste water flow entering the precipitation zone 9 into thin layers, so as to improve the precipitation efficiency.
以上所述仅是本实用新型的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本实用新型技术原理的前提下,还可以做出若干改进和变形,这些改进和变形也应视为本实用新型的保护范围。The above is only the preferred embodiment of the present invention. It should be pointed out that for those skilled in the art, some improvements and deformations can be made without departing from the technical principle of the present invention. These improvements and deformation should also be regarded as the protection scope of the present invention.
Claims (9)
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