CN105780573A - 一种中浓浆泵立管液位自动调节方法 - Google Patents

一种中浓浆泵立管液位自动调节方法 Download PDF

Info

Publication number
CN105780573A
CN105780573A CN201610234694.4A CN201610234694A CN105780573A CN 105780573 A CN105780573 A CN 105780573A CN 201610234694 A CN201610234694 A CN 201610234694A CN 105780573 A CN105780573 A CN 105780573A
Authority
CN
China
Prior art keywords
liquid level
pump
middle underflow
underflow pump
rotating speed
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.)
Granted
Application number
CN201610234694.4A
Other languages
English (en)
Other versions
CN105780573B (zh
Inventor
李军
李智
陈克复
徐峻
莫立焕
冯郁成
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.)
Guangxi Boguan Environmental Products Co ltd
Original Assignee
South China University of Technology SCUT
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 South China University of Technology SCUT filed Critical South China University of Technology SCUT
Priority to CN201610234694.4A priority Critical patent/CN105780573B/zh
Publication of CN105780573A publication Critical patent/CN105780573A/zh
Application granted granted Critical
Publication of CN105780573B publication Critical patent/CN105780573B/zh
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
    • D21C9/10Bleaching ; Apparatus therefor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D15/00Control, e.g. regulation, of pumps, pumping installations or systems
    • F04D15/0066Control, e.g. regulation, of pumps, pumping installations or systems by changing the speed, e.g. of the driving engine
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16KVALVES; TAPS; COCKS; ACTUATING-FLOATS; DEVICES FOR VENTING OR AERATING
    • F16K31/00Actuating devices; Operating means; Releasing devices
    • F16K31/02Actuating devices; Operating means; Releasing devices electric; magnetic
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05DINDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2270/00Control
    • F05D2270/01Purpose of the control system
    • F05D2270/02Purpose of the control system to control rotational speed (n)
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05DINDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2270/00Control
    • F05D2270/70Type of control algorithm
    • F05D2270/706Type of control algorithm proportional-integral-differential

Landscapes

  • Engineering & Computer Science (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Control Of Non-Positive-Displacement Pumps (AREA)
  • Flow Control (AREA)
  • Control Of Positive-Displacement Pumps (AREA)

Abstract

本发明公开了一种中浓浆泵立管液位自动调节方法,通过连锁中浓浆泵转速,泵后阀门开度及下稀释水阀门开关从而控制立管液位。立管液位划分为自我调节区,高液位区,高高液位区,低液位区,低低液位区。自我调节区内阀门开度及转速均保持输入值不变,系统自我整定。高液位区及低液位区内,系统通过PID转速调节;高高液位区及低低液位区内,系统通过PID阀门调节。本发明自动化程度高,无需人员专程看护,能够使得中浓立管稳定在目标液位。

Description

一种中浓浆泵立管液位自动调节方法
技术领域
本发明涉及制浆造纸领域,尤其涉及一种中浓浆泵立管液位自动调节方法。
背景技术
中浓漂白生产过程中,由于来浆流量不稳定或者浓度不稳定,经常造成中浓立管液位波动,对后续生产过程不利。现有自动调节方式主要分为两种,一种为频率调节,即固定阀门开度,根据液位的变化调整电机频率以改变中浓浆泵转速,从而达到调节流量稳定立管液位的目的。但是,当转速降低至一定值时,由于中浓纸浆空气含量高,粘度大,输送阻力大等特点,易出现无法抽送的情况,给生产带来障碍。另一种调节方法为阀门开度调节,即固定中浓浆泵转速,根据液位的变化调整阀门开度从而调整出浆流量以稳定中浓立管液位,但流量变化对阀门开度比较敏感,频繁的调整阀门开度大小,容易造成后续压力和流量的波动,当阀门开度过大时,易造成蒸汽反冲,浆料反冲等生产故障。
发明内容
为克服现有控制系统的弊端,本发明提供一种中浓浆泵立管液位自动调节方法,该方法自动化程度高,控制准确,能快速调整立管液位至目标值。
本发明通过下述技术方案实现:
一种中浓浆泵立管液位自动调节方法,中浓立管4液位自动控制过程通过连锁中浓浆泵转速,泵后阀门2开度及下稀释水阀门3开关从而控制中浓立管4液位;中浓立管4液位划分为自我调节区,高液位区,高高液位区,低液位区,低低液位区;
具体包括如下控制步骤:
步骤1:当液位在自我调节区内,中浓浆泵1转速及泵后阀门2开度均保持原输入值不变;
步骤2:当液位在高液位区内或者低液位区内,通过PID控制系统自动调节中浓浆泵1转速以调节中浓立管4液位至目标液位;
步骤3:当液位在高高液位区,若中浓浆泵1转速未达最大值时,通过PID控制系统自动调节中浓浆泵1转速以调节中浓立管4液位至目标液位;若中浓浆泵1转速达到最大值时,通过PID控制系统自动调节泵后阀门2开度以调节中浓立管4液位至目标液位;
步骤4:当液位在低低液位区时,若中浓泵转速未达最低设定值时,通过PID控制系统自动调节中浓浆泵1转速以调节中浓立管4液位至目标液位;若中浓浆泵1转速达到最低设定值时,通过PID控制系统自动调节泵后阀门2开度以调节中浓立管4液位至目标液位;
步骤5:当液位超过高高液位时,启动高高液位报警;
步骤6:当液位低于低低液位时,启动低低液位报警,并且打开下稀释水阀门3。
还包括一个步骤7,即来浆流量稳定时的控制步骤:当来浆流量稳定时,中浓立管4液位位于b-a自我调节区内,此时,中浓浆泵1转速及泵后阀门2开度均保持原手动输入值不变,当来浆流量突然变大,液位高于a时,在a-aa内时,PID控制系统自动开启中浓浆泵1转速调节,通过增大转速使泵出的流量变大,逐渐降低液位至b-a自我调节区内;当液位增大至aa-aaa高液位区间内时,若中浓浆泵1转速未达到最大值,则继续保持PID转速调节,若转速达到最大值,则保持最大转速开启PID阀门调节,最大阀门开度为40%;当液位降低至a-aa区间时,恢复阀门开度至25%,开启PID转速调节;当液位继续增高至aaa值时,则开启高高位液位报警,操作人员根据现场情况做后续调整;
还包括一个步骤8,即来浆流量变小时的控制步骤:当来浆流量变小,液位低于b时,自动开启PID转速调节,通过降低电机频率降低中浓浆泵1转速,降低泵出流量,使液位逐渐增高至b-a区间内;保证频率最低值不低于33.33HZ,即中浓浆泵1转速不低于2000rpm;若液位持续降低并且低于bb时,则开启PID阀门调节,减小阀门开度,降低泵出流量,使液位逐渐增高至b-bb内;最小阀门开度为15%。若液位持续降低至低于bbb时,开启低低液位报警,并且打开下稀释水阀。
所述中浓浆泵1最低转速为2000rpm。
所述泵后阀门2开度设置在20-40%区间内。
本发明通过连锁中浓浆泵转速,泵后阀门开度及下稀释水阀门开关从而控制立管液位。立管液位划分为自我调节区,高液位区,高高液位区,低液位区,低低液位区。自我调节区内阀门开度及转速均保持输入值不变,系统自我整定。高液位区及低液位区内,系统通过PID转速调节;高高液位区及低低液位区内,系统通过PID阀门调节。本发明技术手段简便易行,自动化程度高,无需人员专程看护,能够使得中浓立管稳定在目标液位。
附图说明
图1为本发明中浓浆泵立管液位自动调节方法示意图;
图中:1-中浓浆泵;2-泵后阀;3-下稀释水阀;4-中浓立管;图中虚线部分为信号连接,实现部分为管路连接。
具体实施方式
下面结合具体实施例对本发明作进一步具体详细描述。
实施例
如图1所示。本发明公开了一种中浓浆泵立管液位自动调节方法,中浓立管4液位自动控制过程通过连锁中浓浆泵转速,泵后阀门2开度及下稀释水阀门3开关从而控制中浓立管4液位;将中浓立管4液位通过刻度方式划分为:自我调节区b-a,高液位区a-aa,高高液位区aa-aaa,低液位区b-bb,低低液位区bb-bbb;可通过如下步骤实现:
步骤1:当液位在自我调节区内,中浓浆泵1转速及泵后阀门2开度均保持原输入值不变;
步骤2:当液位在高液位区内或者低液位区内,通过PID控制系统自动调节中浓浆泵1转速以调节中浓立管4液位至目标液位;
步骤3:当液位在高高液位区,若中浓浆泵1转速未达最大值时,通过PID控制系统自动调节中浓浆泵1转速以调节中浓立管4液位至目标液位;若中浓浆泵1转速达到最大值时,通过PID控制系统自动调节泵后阀门2开度以调节中浓立管4液位至目标液位;
步骤4:当液位在低低液位区时,若中浓泵转速未达最低设定值时,通过PID控制系统自动调节中浓浆泵1转速以调节中浓立管4液位至目标液位;若中浓浆泵1转速达到最低设定值时,通过PID控制系统自动调节泵后阀门2开度以调节中浓立管4液位至目标液位;
步骤5:当液位超过高高液位时,启动高高液位报警;
步骤6:当液位低于低低液位时,启动低低液位报警,并且打开下稀释水阀门3。
当来浆流量稳定时的控制步骤:当来浆流量稳定时,中浓立管4液位位于b-a自我调节区内,此时,中浓浆泵1转速及泵后阀门2开度均保持原手动输入值不变,例如:转速2500rpm,阀门开度25%。当来浆流量突然变大,液位高于a时,在a-aa内时,PID控制系统自动开启中浓浆泵1转速调节,通过增大转速使泵出的流量变大,逐渐降低液位至b-a自我调节区内;当液位增大至aa-aaa高液位区间内时,若中浓浆泵1转速未达到最大值,则继续保持PID转速调节,若转速达到最大值,则保持最大转速开启PID阀门调节,最大阀门开度为40%;当液位降低至a-aa区间时,恢复阀门开度至25%,开启PID转速调节;当液位继续增高至aaa值时,则开启高高位液位报警,操作人员根据现场情况做后续调整;
当来浆流量变小时的控制步骤:当来浆流量变小,液位低于b时,自动开启PID转速调节,通过降低电机频率降低中浓浆泵1转速,降低泵出流量,使液位逐渐增高至b-a区间内;保证频率最低值不低于33.33HZ,即中浓浆泵1转速不低于2000rpm;若液位持续降低并且低于bb时,则开启PID阀门调节,减小阀门开度,降低泵出流量,使液位逐渐增高至b-bb内;最小阀门开度为15%。若液位持续降低至低于bbb时,开启低低液位报警,并且打开下稀释水阀。
所述中浓浆泵1最低转速为2000rpm。
所述泵后阀门2开度设置在20-40%区间内。
如上所述,便可较好地实现本发明。
本发明的实施方式并不受上述实施例的限制,其他任何未背离本发明的精神实质与原理下所作的改变、修饰、替代、组合、简化,均应为等效的置换方式,都包含在本发明的保护范围之内。

Claims (5)

1.一种中浓浆泵立管液位自动调节方法,其特征在于,中浓立管(4)液位自动控制过程通过连锁中浓浆泵转速,泵后阀门(2)开度及下稀释水阀门(3)开关从而控制中浓立管(4)液位;中浓立管(4)液位划分为:自我调节区,高液位区,高高液位区,低液位区,低低液位区;
具体包括如下控制步骤:
步骤(1):当液位在自我调节区内,中浓浆泵(1)转速及泵后阀门(2)开度均保持原输入值不变;
步骤(2):当液位在高液位区内或者低液位区内,通过PID控制系统自动调节中浓浆泵(1)转速以调节中浓立管(4)液位至目标液位;
步骤(3):当液位在高高液位区,若中浓浆泵(1)转速未达最大值时,通过PID控制系统自动调节中浓浆泵(1)转速以调节中浓立管(4)液位至目标液位;若中浓浆泵(1)转速达到最大值时,通过PID控制系统自动调节泵后阀门(2)开度以调节中浓立管(4)液位至目标液位;
步骤(4):当液位在低低液位区时,若中浓泵转速未达最低设定值时,通过PID控制系统自动调节中浓浆泵(1)转速以调节中浓立管(4)液位至目标液位;若中浓浆泵(1)转速达到最低设定值时,通过PID控制系统自动调节泵后阀门(2)开度以调节中浓立管(4)液位至目标液位;
步骤(5):当液位超过高高液位时,启动高高液位报警;
步骤(6):当液位低于低低液位时,启动低低液位报警,并且打开下稀释水阀门(3)。
2.根据权利要求1所述中浓浆泵立管液位自动调节方法,其特征在于,还包括一个步骤(7),即来浆流量稳定时的控制步骤:
当来浆流量稳定时,中浓立管(4)液位位于b-a自我调节区内,此时,中浓浆泵(1)转速及泵后阀门(2)开度均保持原手动输入值不变;当来浆流量突然变大,液位高于a时,在a-aa内时,PID控制系统自动开启中浓浆泵(1)转速调节,通过增大转速使泵出的流量变大,逐渐降低液位至b-a自我调节区内;当液位增大至aa-aaa高液位区间内时,若中浓浆泵(1)转速未达到最大值,则继续保持PID转速调节,若转速达到最大值,则保持最大转速开启PID阀门调节,最大阀门开度为40%;当液位降低至a-aa区间时,恢复阀门开度至25%,开启PID转速调节;当液位继续增高至aaa值时,则开启高高位液位报警,操作人员根据现场情况做后续调整。
3.根据权利要求1所述中浓浆泵立管液位自动调节方法,其特征在于,还包括一个步骤(8),即来浆流量变小时的控制步骤:
当来浆流量变小,液位低于b时,自动开启PID转速调节,通过降低电机频率降低中浓浆泵(1)转速,降低泵出流量,使液位逐渐增高至b-a区间内;保证频率最低值不低于33.33HZ,即中浓浆泵(1)转速不低于2000rpm;若液位持续降低并且低于bb时,则开启PID阀门调节,减小阀门开度,降低泵出流量,使液位逐渐增高至b-bb内;最小阀门开度为15%。若液位持续降低至低于bbb时,开启低低液位报警,并且打开下稀释水阀。
4.根据权利要求1至3中任一项所述中浓浆泵立管液位自动调节方法,其特征在于,所述中浓浆泵(1)最低转速为2000rpm。
5.根据权利要求4所述中浓浆泵立管液位自动调节方法,其特征在于,所述泵后阀门(2)开度设置在20-40%区间内。
CN201610234694.4A 2016-04-14 2016-04-14 一种中浓浆泵立管液位自动调节方法 Active CN105780573B (zh)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610234694.4A CN105780573B (zh) 2016-04-14 2016-04-14 一种中浓浆泵立管液位自动调节方法

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610234694.4A CN105780573B (zh) 2016-04-14 2016-04-14 一种中浓浆泵立管液位自动调节方法

Publications (2)

Publication Number Publication Date
CN105780573A true CN105780573A (zh) 2016-07-20
CN105780573B CN105780573B (zh) 2017-11-07

Family

ID=56396549

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610234694.4A Active CN105780573B (zh) 2016-04-14 2016-04-14 一种中浓浆泵立管液位自动调节方法

Country Status (1)

Country Link
CN (1) CN105780573B (zh)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111448393A (zh) * 2017-11-10 2020-07-24 阿斯彭水泵有限公司 液位传感器
CN112648191A (zh) * 2020-12-22 2021-04-13 杭州玖点轻工机械有限公司 中浓浆泵及其输送系统

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998044188A1 (en) * 1997-04-01 1998-10-08 Ahlström Pumput Oy Method and apparatus for filling a pulp tank
CN101974860A (zh) * 2010-10-26 2011-02-16 华南理工大学 一种中浓打浆泵送方法及装置
CN201843017U (zh) * 2010-10-26 2011-05-25 华南理工大学 一种中浓打浆泵送装置
CN202956673U (zh) * 2012-11-14 2013-05-29 成都卓程科技有限公司 基于单水箱液位的自动控制系统
CN203678038U (zh) * 2013-12-17 2014-07-02 中霖中科环境科技(安徽)股份有限公司 一种水处理砂滤柱的全自动pid水位控制装置

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998044188A1 (en) * 1997-04-01 1998-10-08 Ahlström Pumput Oy Method and apparatus for filling a pulp tank
CN101974860A (zh) * 2010-10-26 2011-02-16 华南理工大学 一种中浓打浆泵送方法及装置
CN201843017U (zh) * 2010-10-26 2011-05-25 华南理工大学 一种中浓打浆泵送装置
CN202956673U (zh) * 2012-11-14 2013-05-29 成都卓程科技有限公司 基于单水箱液位的自动控制系统
CN203678038U (zh) * 2013-12-17 2014-07-02 中霖中科环境科技(安徽)股份有限公司 一种水处理砂滤柱的全自动pid水位控制装置

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111448393A (zh) * 2017-11-10 2020-07-24 阿斯彭水泵有限公司 液位传感器
US11604003B2 (en) 2017-11-10 2023-03-14 Aspen Pumps Limited Liquid level sensor
US11788750B2 (en) 2017-11-10 2023-10-17 Aspen Pumps Limited Liquid level sensor
CN112648191A (zh) * 2020-12-22 2021-04-13 杭州玖点轻工机械有限公司 中浓浆泵及其输送系统

Also Published As

Publication number Publication date
CN105780573B (zh) 2017-11-07

Similar Documents

Publication Publication Date Title
CN105780573A (zh) 一种中浓浆泵立管液位自动调节方法
CN103452608B (zh) 一种用于凝结水系统的控制装置和控制方法
CN204990045U (zh) 一种流体流量/压力控制装置
CN107219758A (zh) 一种汽包液位调节方法
CN107543142A (zh) 一种超临界直流本生锅炉深度调峰优化控制方法
US20190346168A1 (en) Water circulation system for air conditioning system and control method thereof
CN204663594U (zh) 火电厂给水泵汽轮机的给水流量控制系统
CN106086271A (zh) 用于降低高炉鼓风机压缩空气放风量的节能增效的方法
CN107023816A (zh) 锅炉中间点温度的控制方法和控制系统
CN103790059A (zh) 采用中浓浆泵进料的中浓打浆装置及方法
CN114135929B (zh) 多联内机的控制方法、控制装置及空调机组
CN111396298A (zh) 基于压差设定值变化的循环水泵主、被动变频联合控制法
CN203715986U (zh) 一种稳定打浆强度的中浓打浆进料装置
CN203962058U (zh) 一种用于凝结水系统的控制装置
CN205781167U (zh) 动态平衡电动调节阀
KR101945413B1 (ko) 압축기 제어 시스템 및 압축기의 제어 방법
CN207813844U (zh) 一种自动启停水泵装置
KR20200055338A (ko) 듀얼 pid 압력 제어를 적용한 원유생산시스템
CN205295784U (zh) 一种用于造纸上浆的稀释水系统
JPH0350919B2 (zh)
RU2659348C1 (ru) Устройство регулирования давления газа
CN103528045B (zh) 一种锅炉水位过零控制方法
CN107893751B (zh) 一种基于多泵联动的泵运行调控方法
CN105558745A (zh) 一种杀菌机脱气罐内的液位控制方法
CN204294133U (zh) 一种灰库加湿搅拌机及其供水装置

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20190920

Address after: 510640 Tianhe District, Guangdong, No. five road, No. 381,

Co-patentee after: Chen Kefu

Patentee after: Li Jun

Co-patentee after: Guangzhou South China University of Technology science and Technology Park Co.,Ltd.

Address before: 510640 Tianhe District, Guangdong, No. five road, No. 381,

Patentee before: South China University of Technology

TR01 Transfer of patent right

Effective date of registration: 20191212

Address after: 528000 room 409, block 22, Shunlian Machinery City, No. 18, Xingye 4th Road, Guanglong Industrial Park, Chihua neighborhood committee, Chencun Town, Shunde District, Foshan City, Guangdong Province

Co-patentee after: Guangzhou South China University of Technology science and Technology Park Co.,Ltd.

Patentee after: Foshan dongyuxing Technical Service Co.,Ltd.

Address before: 510640 Tianhe District, Guangdong, No. five road, No. 381,

Co-patentee before: Chen Kefu

Patentee before: Li Jun

Co-patentee before: Guangzhou South China University of Technology science and Technology Park Co.,Ltd.

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20191226

Address after: 528000 room 410, block 22, Shunlian Machinery City, No. 18, Xingye 4th Road, Guanglong Industrial Park, Chihua neighborhood committee, Chencun Town, Shunde District, Foshan City, Guangdong Province

Patentee after: Foshan xinzhidao Environmental Protection Technology Co.,Ltd.

Address before: 528000 room 409, block 22, Shunlian Machinery City, No. 18, Xingye 4th Road, Guanglong Industrial Park, Chihua neighborhood committee, Chencun Town, Shunde District, Foshan City, Guangdong Province

Co-patentee before: Guangzhou South China University of Technology science and Technology Park Co.,Ltd.

Patentee before: Foshan dongyuxing Technical Service Co.,Ltd.

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20240419

Address after: 546300 Luodong Industrial Park, Yizhou District, Hechi City, Guangxi Zhuang Autonomous Region

Patentee after: GUANGXI BOGUAN ENVIRONMENTAL PRODUCTS Co.,Ltd.

Country or region after: China

Address before: 528000 room 410, block 22, Shunlian Machinery City, No. 18, Xingye 4 road, Guanglong Industrial Park, Chihua neighborhood committee, Chencun Town, Shunde District, Foshan City, Guangdong Province

Patentee before: Foshan xinzhidao Environmental Protection Technology Co.,Ltd.

Country or region before: China

TR01 Transfer of patent right