WO2023246150A1 - 一种氢电导表树脂再生系统及再生方法 - Google Patents
一种氢电导表树脂再生系统及再生方法 Download PDFInfo
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- WO2023246150A1 WO2023246150A1 PCT/CN2023/078154 CN2023078154W WO2023246150A1 WO 2023246150 A1 WO2023246150 A1 WO 2023246150A1 CN 2023078154 W CN2023078154 W CN 2023078154W WO 2023246150 A1 WO2023246150 A1 WO 2023246150A1
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- Prior art keywords
- resin
- regeneration
- hydrochloric acid
- water
- conductivity meter
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- 239000011347 resin Substances 0.000 title claims abstract description 140
- 229920005989 resin Polymers 0.000 title claims abstract description 140
- 238000011069 regeneration method Methods 0.000 title claims abstract description 123
- 230000008929 regeneration Effects 0.000 title claims abstract description 115
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 32
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 32
- 239000001257 hydrogen Substances 0.000 title claims abstract description 32
- 238000000034 method Methods 0.000 title claims description 17
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 162
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 86
- 239000002253 acid Substances 0.000 claims abstract description 60
- 239000000523 sample Substances 0.000 claims abstract description 22
- 238000011010 flushing procedure Methods 0.000 claims abstract description 21
- 238000012544 monitoring process Methods 0.000 claims abstract description 8
- 238000010612 desalination reaction Methods 0.000 claims description 12
- 230000001105 regulatory effect Effects 0.000 claims description 10
- 230000001276 controlling effect Effects 0.000 claims description 4
- 239000003814 drug Substances 0.000 claims description 3
- 238000011033 desalting Methods 0.000 abstract 1
- 238000012423 maintenance Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 3
- 239000003729 cation exchange resin Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000002955 isolation Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000012797 qualification Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J49/00—Regeneration or reactivation of ion-exchangers; Apparatus therefor
- B01J49/05—Regeneration or reactivation of ion-exchangers; Apparatus therefor of fixed beds
- B01J49/09—Regeneration or reactivation of ion-exchangers; Apparatus therefor of fixed beds of mixed beds
Definitions
- the publication number is CN112808324A "Hydrogen-type cation exchange resin column dynamic regeneration device and its operating method", which specifically discloses the dynamic regeneration of hydrogen-type cation exchange resin by setting up an acid storage tank, a desalted water tank, and a cation exchange resin column.
- the acid regeneration solution is prepared in advance for this device, and during the regeneration process, there may be uneven acid concentration. The instability of the acid concentration will have a negative impact on the degree of resin regeneration. .
- the invention provides a hydrogen conductivity meter resin regeneration system, which includes a resin regeneration system connected to the original mixed bed system and a resin regeneration flushing and water replenishing system for monitoring and controlling the resin regeneration system; the resin regeneration system includes interconnected hydrochloric acid adding systems.
- the main pipe connecting the hydrochloric acid dosing box and the regenerated resin cylinder is divided into two branches, one is connected to the acid inlet at the bottom of the regenerated resin cylinder, and the other is connected to the water inlet at the top of the regenerated resin cylinder; with the acid inlet
- a drainage pipeline is installed in parallel on the branch connected to the water inlet; an acid discharge pipeline is installed in parallel on the branch connected to the water inlet; valves are installed on all pipelines.
- a regulating dosing pump is provided on the main pipe connecting the hydrochloric acid dosing box and the regenerated resin cylinder, and at the same time, the main pipe is connected to the acidometer.
- the solenoid valve has two channels, one channel is connected to the water pipeline of the desalination regeneration water pump of the original mixed bed system, and the other channel is connected to the water inlet pipe to replenish the hydrochloric acid dosing tank.
- the probe assembly includes at least three probes, which are respectively located at the high, middle and low water levels in the hydrochloric acid dosing tank, and the low water level is located at the bottom of the hydrochloric acid dosing tank.
- the regenerated resin cylinder is a sealed cylinder with a cover, the lower part of the side wall of the cylinder is provided with an acid inlet, the upper part is provided with a water inlet, and filter cloths are provided at both the acid inlet and the water inlet.
- the hydrogen conductivity meter resin regeneration method includes the following steps:
- hydrochloric acid regenerates the resin in step S4
- hydrochloric acid enters the regenerated resin cylinder through the hydrochloric acid dosing box, and its flow direction is downward in and up out
- desalted water rinses the resin in step S5
- desalted water is added through hydrochloric acid.
- the box enters the recycled resin cylinder, and its flow direction is up, in, and down.
- the invention provides a hydrogen conductivity meter resin regeneration system.
- the hydrogen conductivity meter is directly connected to the original mixed bed system through pipelines.
- the acidity meter and conductivity meter of the original mixed bed system can control the regeneration of the entire resin regeneration process.
- the acid concentration and regeneration end point can simultaneously ensure the stability of the acid concentration during the regeneration process, and overcome the technical problems in the existing technology such as the need to purchase a special regeneration device, the difficulty in controlling the instrument parameters of the regeneration process, and the inability to monitor the qualified end point of regeneration.
- the system of the present invention uses As well as low price and cost, compared to the specialized hydrogen conductivity meter resin regeneration equipment on the market, the cost of this device is reduced to 1/90 of the specialized hydrogen conductivity meter resin regeneration equipment, and it is easy to maintain.
- acid regeneration is used to adopt a bottom-in-top-out acid flow route to ensure that the resin is completely in contact with the regeneration acid and the degree of regeneration is ensured.
- Figure 1 is a schematic diagram of the connection between the Zhongyuan mixed bed system and the resin regeneration system of the present invention
- Figure 2 is a schematic diagram of the pipeline connection of the resin regeneration system in the present invention.
- Figure 3 is a schematic connection diagram of the resin regeneration flushing and water replenishing system in the present invention.
- a hydrogen conductivity meter resin regeneration system including a resin regeneration system connected to the original mixed bed system 6 and a resin regeneration flushing and water supply system for monitoring and controlling the resin regeneration system.
- the resin regeneration system controls the regeneration through the control of hydrochloric acid solution.
- the resin is subjected to acid regeneration treatment, and the resin regeneration flushing and water replenishing system controls water inflow after the acid regeneration treatment to flush the regenerated resin;
- the resin regeneration system includes an interconnected hydrochloric acid dosing tank 1 and a regenerated resin cylinder 2;
- the resin regeneration flushing and water replenishing system includes a host computer, a solenoid valve and a probe assembly that are electrically connected to each other; the acid inlet at the bottom of the regenerated resin cylinder 2 A passage is introduced to be directly connected to the conductivity meter of the original mixed bed system 6, and a passage is introduced to the pipeline connecting the regenerated resin cylinder 2 and the hydrochloric acid dosing tank 1 to be connected to the acidometer 3 of the original mixed bed system 6, thereby directly connecting the resin regeneration system Connect to the original mixed bed system 6; the solenoid valve 5 is set on the water pipeline of the desalination regeneration water pump of the original mixed bed system 6 to control the water replenishment of the hydrochloric acid dosing tank 1.
- the host is electrically connected to the solenoid valve and the probe assembly respectively.
- the main pipe connecting the hydrochloric acid dosing box 1 and the regenerated resin cylinder 2 is divided into two branches. One is connected to the acid inlet at the bottom of the regenerated resin cylinder 2. There is a No. 7 valve on the pipeline, and the other is connected to the regenerated resin.
- the water inlet at the top of barrel 2 is connected, and a No. 6 valve is provided on the pipeline; a drainage pipeline is arranged in parallel on the branch connecting the hydrochloric acid dosing box 1 and the acid inlet, and a No. 8 valve is arranged on the drainage pipeline.
- valve No. 2 the pipeline connecting the conductivity meter 4 with the original mixed bed system 6 is provided with valve No. 2; hydrochloric acid dosing box 1.
- An acid discharge pipeline is arranged in parallel on the branch road connected to the water inlet, and a No. 5 valve is provided on the acid discharge pipeline; a regulating dosing pump is provided on the main pipeline connected to the hydrochloric acid dosing box 1 and the recycled resin cylinder 2, and a regulating dosing pump is installed on the main pipeline.
- the pipeline connected to the acidometer 3 is equipped with a No. 3 valve on the main pipeline connected to the acidometer 3, and a No.
- the regenerated resin cylinder 2 is with
- the sealing cylinder of the cover and the acid inlet of the regenerated resin cylinder 2 can also be the drain port in the flushing and replenishing process, and the water inlet can also be the acid discharge port in the acid regeneration stage.
- the acid inlet and the water inlet are both equipped with filter cloths.
- the solenoid valve 5 is installed on the resin regeneration flushing and water replenishing system to have two channels. One channel is connected to the water pipeline of the desalination regeneration water pump of the original mixed bed system 6, and the other channel is connected to the water inlet pipe to replenish the hydrochloric acid dosing tank 1. , and then during the flushing and water replenishing stage, the desalted regeneration water is controlled to enter the hydrochloric acid dosing tank 1 for flushing preparation of the regenerated resin.
- the probe assembly includes at least three probes, which are respectively located at the high, medium and low water levels in the hydrochloric acid dosing box 1.
- the low water level is located at the bottom of the hydrochloric acid dosing box 1.
- the probe transmits a signal to the host, and the host controls the solenoid valve to close and stop supplying water to the hydrochloric acid dosing tank 1.
- the host controls the solenoid valve to open and continue to supply water to the hydrochloric acid dosing tank.
- a hydrogen conductivity meter resin regeneration method includes the following steps:
- the flushing phase begins. Open the solenoid valve 5 to replenish the hydrochloric acid dosing tank 1. After replenishing to a certain height, close the solenoid valve 5 and open No. 6 valve, No. 8 valve, No. 1 valve and solenoid valve 5. , close the No. 5 valve, No. 7 valve and No. 3 valve.
- the desalted water enters the regenerated resin cylinder 2 from the hydrochloric acid dosing tank 1 through the water inlet at the top of the regenerated resin cylinder 2.
- the regenerated resin in the cylinder is flushed.
- the desalted water is The flow direction is up, in, and out. During the flushing process, observe that the conductivity meter 4 rushes below 1us/cm, and the resin regeneration is qualified.
- hydrochloric acid regenerates the resin in step S4
- the hydrochloric acid enters the regenerated resin cylinder 2 through the hydrochloric acid dosing box 1, and its flow direction is downward in and up out
- the desalted water rinses the resin in step S5
- the desalted water passes through the hydrochloric acid
- the dosing box 1 enters the recycled resin cylinder 2, and its flow direction is up, in, and down.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treatment Of Water By Ion Exchange (AREA)
- Investigating Or Analyzing Materials By The Use Of Electric Means (AREA)
Abstract
本发明具体公开一种氢电导表树脂再生系统，包括与原混床系统连接的树脂再生系统以及用于监测和控制树脂再生系统的树脂再生冲洗补水系统；所述树脂再生系统包括相互连通的盐酸加药箱和再生树脂筒；所述树脂再生冲洗补水系统包括相互电连接的主机、电磁阀和探头组件；所述再生树脂筒底部进酸口引一通路直接与原混床系统的电导率表连接，所述再生树脂筒与盐酸加药箱连通的管路上引一通路与原混床系统的酸度计连接，进而将树脂再生系统直接接入原混床系统；所述电磁阀设置在原混床系统的除盐再生水泵来水管路上，控制对盐酸加药箱的补水，主机分别与电磁阀和探头组件电连接。
Description
本发明属于电力技术中化学仪表维护技术领域，具体涉及一种氢电导表树脂再生系统及再生方法。
化学仪表维护一种是电厂维护专业的一大难题，尤其是对氢在线仪表的检测和维护。氢树脂柱的树脂再生不够彻底，会导致在线氢电导率波动较大，无法准确监测水质。现有技术中，为了节约维护成本，大部分电厂未采购专用的树脂再生仪器，只是让化验班组将氢树脂柱浸泡在装有盐酸水溶液的容器中，或者是用流水对氢树脂柱表面进行冲洗，但是，上述做法存在树脂再生酸浓度无法检测的问题，同时冲洗过程中，水从上部进下部排，仅是冲洗了树脂表面，树脂再生不彻底，再生过程中无法监测再生合格重点等问题。
公开号为CN112808324A“氢型阳离子交换树脂柱动态再生装置及其操作方法”，其中具体公开了通过设置酸液储箱、除盐水箱、阳离子交换树脂柱，实现对氢型阳离子交换树脂动态再生，无需现场实时监视，提高了再生效率高，但是，该装置是提前配好酸再生溶液，而且再生过程中，可能存在酸浓度不均现象，酸浓度的不稳定，会对树脂再生度产生不良影响。
为了解决上述技术问题，本发明提供一种氢电导表树脂再生系统及再生方法，利用原有混床再生酸度计和电导率表，有效控制再生过程中酸浓度以及再生终点。
本发明的技术方案如下：
本发明提供一种氢电导表树脂再生系统，包括与原混床系统连接的树脂再生系统以及用于监测和控制树脂再生系统的树脂再生冲洗补水系统；所述树脂再生系统包括相互连通的盐酸加药箱和再生树脂筒；所述树脂再生冲洗补水系统包括相互电连接的主机、电磁阀和探头组件；所述再生树脂筒底部进酸口引一通路直接与原混床系统的电导率表连接，所述再生树脂筒与盐酸加药箱连通的管路上引一通路与原混床系统的酸度计连接，进而将树脂再生系统直接接入原混床系统；所述电磁阀设置在原混床系统的除盐再生水泵来水管路上，控制对盐酸加药箱的补水，主机分别与电磁阀和探头组件电连接。
进一步的，所述盐酸加药箱与再生树脂筒连通的主管路上分出两条支路，一条与再生树脂筒底部的进酸口连通，一条与再生树脂筒顶部的进水口连通；与进酸口连通的支路上并联设置排水管路；与进水口连通的支路上并联设置排酸管路；所有管路上均设置阀门。
进一步的，所述盐酸加药箱与再生树脂筒连通的主管路上设置有调节加药泵，同时主管路与酸度计连通。
进一步的，所述电磁阀为两通路，一通路与原混床系统的除盐再生水泵来水管路连接，另一通路连接进水管对盐酸加药箱进行补水。
进一步的，所述探头组件包括至少三个探头，分别位于盐酸加药箱中的高、中、低水位线处，低水位线位于盐酸加药箱底部。
进一步的，所述探头组件与主机连接时将若干探头线进行合并，形成两根信号输出线，分别传输高、中水位示警信号。
进一步的，所述再生树脂筒为带盖的密封筒，筒体侧壁的下部设置有进酸口，上部设置有进水口，且进酸口和进水口处均设置有滤布。
本发明还提供一种氢电导表树脂再生方法，利用上述氢电导表树脂再生系统实现氢电导表的树脂交换柱再生。
进一步的，所述氢电导表树脂再生方法包括如下步骤：
S1、根据替换的再生树脂量计算出再生树脂的盐酸用量，将盐酸加入盐酸加药箱；
S2、根据盐酸加药箱中盐酸的体积，向盐酸加药箱内添加除盐水，使盐酸加药箱中酸浓度达到5%；
S3、将设置在原混床系统的酸度计、电导率表与原混床系统的酸再生管路隔离；
S4、将酸度计与加药调节泵之间连通，启动加药调节泵，在加药调节泵驱的作用下，盐酸加药箱中的盐酸经由再生树脂筒底部的进酸口进入筒内流经再生树脂，实现再生；同时实时根据酸度计的参数，调整加药调节泵频率，使酸度计的监测参数接近再生酸度；
S5、进酸结束后，连通除盐再生水泵与盐酸加药箱，除盐水经由再生树脂筒顶部的进水口接入除盐再生水对筒内的再生树脂进行冲洗，冲洗过程中，观察电导率表表冲至1us/cm以下，树脂再生合格。
进一步的，所述步骤S4中盐酸再生树脂时，盐酸经由盐酸加药箱进入再生树脂筒，其流动方向为下进上出；所述步骤S5中除盐水冲洗树脂时，除盐水经由盐酸加药箱进入再生树脂筒，其流动方向为上进下出。
相较于现有技术，本发明的有益效果在于：
本发明提供一种氢电导表树脂再生系统，将氢电导表通过管路直接接入原有的混床系统，通过原有混床系统的酸度计和电导表能够控制树脂再生工艺整个过程的再生酸浓度和再生终点，同时能够保证再生过程酸浓度稳定，克服了现有技术中需要购置专门的再生装置以及再生过程仪器参数不好控制、无法监控再生合格终点等技术问题，本发明的系统使用以及价格成本低，针对市场上专门的氢电导表树脂再生设备，本装置成本降为专门的氢电导表树脂再生设备的1/90，同时检修方便。
本发明的树脂再生过程中利用酸再生采用下进上出的酸流动路线，保证树脂完全与再生酸接触，保证再生度。
（3）利用本发明提供的再生系统进行树脂再生能够减少人员操作，再生冲洗时，原方法需要一直工人搅拌，而本发明只需要电磁阀进行补水，下部进水，将树脂筒内残留酸从上部排出，直至冲洗干净。
图1为本发明中原混床系统与树脂再生系统连接示意图；
图2为本发明中树脂再生系统的管路连接示意图；
图3为本发明中树脂再生冲洗补水系统的连接示意图；
图中附图标记表示：
1、盐酸加药箱；2、再生树脂筒；3、酸度计；4、电导率表；5、电磁阀；6、原混床系统。
下面结合附图和较佳实施例对本发明做进一步的说明。
一种氢电导表树脂再生系统，包括与原混床系统6连接的树脂再生系统以及用于监测和控制树脂再生系统的树脂再生冲洗补水系统，所述树脂再生系统通过盐酸溶液的控制，对再生树脂进行酸再生处理，所述树脂再生冲洗补水系统在酸再生处理过后控制进水，对再生树脂进行冲洗；
所述树脂再生系统包括相互连通的盐酸加药箱1和再生树脂筒2；所述树脂再生冲洗补水系统包括相互电连接的主机、电磁阀和探头组件；所述再生树脂筒2底部进酸口引一通路直接与原混床系统6的电导表连接，再生树脂筒2与盐酸加药箱1连通的管路上引一通路与原混床系统6的酸度计3连接，进而将树脂再生系统直接接入原混床系统6；所述电磁阀5设置在原混床系统6的除盐再生水泵来水管路上，控制对盐酸加药箱1的补水，主机分别与电磁阀和探头组件电连接。
其中，所述盐酸加药箱1与再生树脂筒2连通的主管路上分出两条支路，一条与再生树脂筒2底部的进酸口连通，管路上设置有7号阀门，一条与再生树脂筒2顶部的进水口连通，管路上设置有6号阀门；盐酸加药箱1与进酸口连通的支路上并联设置排水管路，排水管路上设置有8号阀门，从排水管路上引出所述与原混床系统6的电导率表4连接的通路，此通路上设置有1号阀门，同时电导率表4与原混床系统6连通的管路上设置于2号阀门；盐酸加药箱1与进水口连通的支路上并联设置排酸管路，排酸管路上设置有5号阀门；所述盐酸加药箱1与再生树脂筒2连通的主管路上设置有调节加药泵，同时主管路与酸度计3连通，主管路与酸度计3连通的管路上设置有3号阀门，酸度计3与原混床系统6连通的管路上设置有4号阀门；所述再生树脂筒2为带盖的密封筒，再生树脂筒2的进酸口也可为冲洗补水过程中的排水口，进水口也可为酸再生阶段的排酸口，进酸口和进水口处均设置有滤布。
其中，所述树脂再生冲洗补水系统上设置电磁阀5为两通路，一通路与原混床系统6的除盐再生水泵来水管路连接，另一通路连接进水管对盐酸加药箱1进行补水，进而在冲洗补水阶段，控制除盐再生水进入盐酸加药箱1中进行再生树脂的冲洗准备。
其中，所述探头组件包括至少三个探头，分别位于盐酸加药箱1中的高、中、低水位线处，低水位线位于盐酸加药箱1底部，当盐酸加药箱1的水位接触到位于高水位的上探头时，探头传输信号至主机，主机控制电磁阀关闭，停止向盐酸加药箱1供水，当盐酸加药箱1的水位低于位于中水位的探头时，此时只有低水位线的下探头能够感受，输出信号至主机，主机控制电磁阀开启，继续向盐酸加药箱供水。
一种氢电导表树脂再生方法，包括如下步骤：
S1、根据替换的再生树脂量计算出再生树脂的盐酸用量，将盐酸加入盐酸加药箱；
S2、根据盐酸加药箱1中盐酸的体积，向盐酸加药箱1内添加除盐水，使盐酸加药箱1中酸浓度达到5%；
S3、将设置在原混床系统6的酸度计3、电导率表4与原混床系统6的酸再生管路隔离；在本实施例中，关闭酸度计3与原混床系统6连通管路上的4号阀门的开关实现酸度计3与原酸再生管路的隔离，关闭电导率表4与原混床系统6连通管路上的2号阀门实现电导率表4与原酸再生管路的隔离；
S4、进酸，此时开启5号阀门、7号阀门和3号阀门，关闭6号阀门、8号阀门和1号阀门，将酸度计3与加药调节泵之间连通，盐酸加药箱1与再生树脂筒2连通，启动加药调节泵，在加药调节泵驱的作用下，盐酸加药箱1中的盐酸经由再生树脂筒2底部的进酸口进入筒内流经再生树脂，再经由树脂再生筒2顶部的排酸口流出，实现树脂再生，酸溶液的流动方式为下进上出，保证树脂完全与再生酸接触，保证再生度；同时实时根据酸度计3的参数，调整加药调节泵频率，使酸度计3的监测参数接近再生酸度；
S5、进酸结束后开始冲洗阶段，打开电磁阀5，对盐酸加药箱1进行补水，补至一定高度后电磁阀5关闭，开启6号阀门、8号阀门和1号阀门以及电磁阀5，关闭，5号阀门、7号阀门和3号阀，除盐水由盐酸加药箱1经由再生树脂筒2顶部的进水口进入再生树脂筒2，对筒内的再生树脂进行冲洗，除盐水的流动方向为上进下出，冲洗过程中，观察电导率表表4冲至1us/cm以下，树脂再生合格。
进一步的，所述步骤S4中盐酸再生树脂时，盐酸经由盐酸加药箱1进入再生树脂筒2，其流动方向为下进上出；所述步骤S5中除盐水冲洗树脂时，除盐水经由盐酸加药箱1进入再生树脂筒2，其流动方向为上进下出。
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他相关的技术领域，均同理包括在本发明的专利保护范围内。
Claims (10)
- 一种氢电导表树脂再生系统，其特征在于：包括与原混床系统（6）连接的树脂再生系统以及用于监测和控制树脂再生系统的树脂再生冲洗补水系统；所述树脂再生系统包括相互连通的盐酸加药箱（1）和再生树脂筒（2）；所述树脂再生冲洗补水系统包括相互电连接的主机、电磁阀和探头组件；所述再生树脂筒（2）底部进酸口引一通路直接与原混床系统（6）的电导率表（4）连接，所述再生树脂筒（2）与盐酸加药箱（1）连通的管路上引一通路与原混床系统（6）的酸度计连接，进而将树脂再生系统直接接入原混床系统（6）；所述电磁阀（5）设置在原混床系统（6）的除盐再生水泵来水管路上，控制对盐酸加药箱（1）的补水，主机分别与电磁阀（5）和探头组件电连接。
- 如权利要求1所述的一种氢电导表树脂再生系统，其特征在于：所述盐酸加药箱（1）与再生树脂筒（2）连通的主管路上分出两条支路，一条与再生树脂筒（2）底部的进酸口连通，一条与再生树脂筒（2）顶部的进水口连通；与进酸口连通的支路上并联设置排水管路；与进水口连通的支路上并联设置排酸管路；所有管路上均设置阀门。
- 如权利要求2所述的一种氢电导表树脂再生系统，其特征在于：所述盐酸加药箱（1）与再生树脂筒（2）连通的主管路上设置有调节加药泵，同时主管路与酸度计（3）连通。
- 如权利要求3所述的一种氢电导表树脂再生系统，其特征在于：所述电磁阀（5）为两通路，一通路与原混床系统（6）的除盐再生水泵来水管路连接，另一通路连接进水管对盐酸加药箱（1）进行补水。
- 如权利要求4所述的一种氢电导表树脂再生系统，其特征在于：所述探头组件包括至少三个探头，分别位于盐酸加药箱（1）中的高、中、低水位线处，低水位线位于盐酸加药箱（1）底部。
- 如权利要求5所述的一种氢电导表树脂再生系统，其特征在于：所述探头组件与主机连接时将若干探头线进行合并，形成两根信号输出线，分别传输高、中水位示警信号。
- 如权利要求6所述的一种氢电导表树脂再生系统，其特征在于：所述再生树脂筒（2）为带盖的密封筒，筒体侧壁的下部设置有进酸口，上部设置有进水口，且进酸口和进水口处均设置有滤布。
- 一种氢电导表树脂再生方法，其特征在于：利用如权利要求1至6任一所述的氢电导表树脂再生系统实现氢电导表的树脂交换柱再生。
- 如权利要求8所述的一种氢电导表树脂再生方法，其特征在于，包括如下步骤：S1、根据替换的再生树脂量计算出再生树脂的盐酸用量，将盐酸加入盐酸加药箱（1）；S2、根据盐酸加药箱（1）中盐酸的体积，向盐酸加药箱（1）内添加除盐水，使盐酸加药箱（1）中酸浓度达到5%；S3、将设置在原混床系统（6）的酸度计（3）、电导率表（4）与原混床系统（6）的酸再生管路隔离；S4、将酸度计与加药调节泵之间连通，启动加药调节泵，在加药调节泵驱的作用下，盐酸加药箱（1）中的盐酸经由再生树脂筒（2）底部的进酸口进入筒内流经再生树脂，实现再生；同时实时根据酸度计的参数，调整加药调节泵频率，使酸度计的监测参数接近再生酸度；S5、进酸结束后，连通除盐再生水泵与盐酸加药箱（1），除盐水经由再生树脂筒（2）顶部的进水口接入除盐再生水对筒内的再生树脂进行冲洗，冲洗过程中，观察电导率表（4）表冲至1us/cm以下，树脂再生合格。
- 如权利要求9所述的一种氢电导表树脂再生方法，其特征在于：所述步骤S4中盐酸再生树脂时，盐酸经由盐酸加药箱（1）进入再生树脂筒（2），其流动方向为下进上出；所述步骤S5中除盐水冲洗树脂时，除盐水经由盐酸加药箱（1）进入再生树脂筒（2），其流动方向为上进下出。
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Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001232217A (ja) * | 2000-02-25 | 2001-08-28 | Japan Organo Co Ltd | イオン交換樹脂の再生法 |
| KR100578553B1 (ko) * | 2005-01-28 | 2006-05-12 | 한국정수공업 주식회사 | 이온교환수지의 전기식 재생 장치 및 공정 |
| CN201832658U (zh) * | 2010-09-21 | 2011-05-18 | 华北电力科学研究院有限责任公司 | 电导率表氢柱再生装置 |
| CN204911543U (zh) * | 2015-08-17 | 2015-12-30 | 南京华天科技发展股份有限公司 | 一种氢电导率测量用阳离子交换树脂的再生装置 |
| CN112808325A (zh) * | 2021-02-01 | 2021-05-18 | 国投钦州发电有限公司 | 氢型阳离子交换树脂再生装置及其操作方法 |
| CN216573132U (zh) * | 2021-08-19 | 2022-05-24 | 华电电力科学研究院有限公司 | 一种离子交换树脂动态再生装置 |
| US20220168725A1 (en) * | 2019-03-04 | 2022-06-02 | Ionx Solutions, Llc | System and method for regenerating and restoring kinetic properties of resin |
| CN114618596A (zh) * | 2021-12-16 | 2022-06-14 | 华润电力（贺州）有限公司 | 一种在线氢电导率表树脂再生装置及树脂再生方法 |
| CN217189629U (zh) * | 2021-12-16 | 2022-08-16 | 华润电力（贺州）有限公司 | 一种在线氢电导率表树脂自动再生装置 |
| CN115007225A (zh) * | 2022-06-20 | 2022-09-06 | 华能(福建漳州)能源有限责任公司 | 一种氢电导表树脂再生系统及再生方法 |
| CN219031837U (zh) * | 2022-12-29 | 2023-05-16 | 哈尔滨安泰利达科技开发有限公司 | 氢导树脂再生系统 |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN207401488U (zh) * | 2017-10-16 | 2018-05-25 | 中国大唐集团科学技术研究院有限公司华中分公司 | 一种在线化学仪表阳离子交换柱自动再生装置 |
| CN207483495U (zh) * | 2017-10-18 | 2018-06-12 | 辽宁莱特莱德环境工程有限公司 | 一种过氧乙酸废水回收处理装置 |
| CN109569745A (zh) * | 2018-12-06 | 2019-04-05 | 中电环保股份有限公司 | 阳离子交换树脂自动再生装置及方法 |
| CN210642009U (zh) * | 2019-08-13 | 2020-06-02 | 姚惠荣 | 一种鱼缸自动换水补水系统 |
| CN213803032U (zh) * | 2020-09-29 | 2021-07-27 | 华能山东发电有限公司白杨河发电厂 | 一种可再生的发电机内冷水处理装置 |
-
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- 2022-06-20 CN CN202210697450.5A patent/CN115007225B/zh active Active
-
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- 2023-02-24 JP JP2023539258A patent/JP2024526488A/ja active Pending
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Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001232217A (ja) * | 2000-02-25 | 2001-08-28 | Japan Organo Co Ltd | イオン交換樹脂の再生法 |
| KR100578553B1 (ko) * | 2005-01-28 | 2006-05-12 | 한국정수공업 주식회사 | 이온교환수지의 전기식 재생 장치 및 공정 |
| CN201832658U (zh) * | 2010-09-21 | 2011-05-18 | 华北电力科学研究院有限责任公司 | 电导率表氢柱再生装置 |
| CN204911543U (zh) * | 2015-08-17 | 2015-12-30 | 南京华天科技发展股份有限公司 | 一种氢电导率测量用阳离子交换树脂的再生装置 |
| US20220168725A1 (en) * | 2019-03-04 | 2022-06-02 | Ionx Solutions, Llc | System and method for regenerating and restoring kinetic properties of resin |
| CN112808325A (zh) * | 2021-02-01 | 2021-05-18 | 国投钦州发电有限公司 | 氢型阳离子交换树脂再生装置及其操作方法 |
| CN216573132U (zh) * | 2021-08-19 | 2022-05-24 | 华电电力科学研究院有限公司 | 一种离子交换树脂动态再生装置 |
| CN114618596A (zh) * | 2021-12-16 | 2022-06-14 | 华润电力（贺州）有限公司 | 一种在线氢电导率表树脂再生装置及树脂再生方法 |
| CN217189629U (zh) * | 2021-12-16 | 2022-08-16 | 华润电力（贺州）有限公司 | 一种在线氢电导率表树脂自动再生装置 |
| CN115007225A (zh) * | 2022-06-20 | 2022-09-06 | 华能(福建漳州)能源有限责任公司 | 一种氢电导表树脂再生系统及再生方法 |
| CN219031837U (zh) * | 2022-12-29 | 2023-05-16 | 哈尔滨安泰利达科技开发有限公司 | 氢导树脂再生系统 |
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