[go: up one dir, main page]

CN104888866B - A kind of silicon magnesium complexes carrier and preparation method thereof - Google Patents

A kind of silicon magnesium complexes carrier and preparation method thereof Download PDF

Info

Publication number
CN104888866B
CN104888866B CN201510258411.5A CN201510258411A CN104888866B CN 104888866 B CN104888866 B CN 104888866B CN 201510258411 A CN201510258411 A CN 201510258411A CN 104888866 B CN104888866 B CN 104888866B
Authority
CN
China
Prior art keywords
magnesium
silicon
carrier
concentration
aluminum
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
Application number
CN201510258411.5A
Other languages
Chinese (zh)
Other versions
CN104888866A (en
Inventor
王爱菊
苏本章
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.)
JUANCHENG DINGSHENG CHEMICAL TECHNOLOGY Co.,Ltd.
Original Assignee
Juancheng Ruiding Technology Co Ltd
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 Juancheng Ruiding Technology Co Ltd filed Critical Juancheng Ruiding Technology Co Ltd
Priority to CN201510258411.5A priority Critical patent/CN104888866B/en
Publication of CN104888866A publication Critical patent/CN104888866A/en
Application granted granted Critical
Publication of CN104888866B publication Critical patent/CN104888866B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Catalysts (AREA)

Abstract

本发明涉及一种催化剂载体,特别涉及一种硅镁复合物载体及其制备方法。该硅镁复合物载体由硅、铝的氧化物和镁的碳酸盐及其氧化物的复合物,或硅的氧化物和镁的碳酸盐及其氧化物的复合物为载体,其中Si:Al:Mg=5‑7:0‑3:2‑5;本发明制备方法简单,并且活性高,强度高,选择性好;并且本发明采用共沉淀法制得载体,增大了载体的比表面积和细孔容积。The invention relates to a catalyst carrier, in particular to a silicon-magnesium composite carrier and a preparation method thereof. The silicon-magnesium composite carrier is supported by a composite of silicon, aluminum oxide, magnesium carbonate and its oxide, or a composite of silicon oxide, magnesium carbonate and its oxide, wherein Si : Al: Mg=5-7:0-3:2-5; the preparation method of the present invention is simple, and has high activity, high strength, and good selectivity; surface area and pore volume.

Description

一种硅镁复合物载体及其制备方法A kind of silicon-magnesium composite carrier and preparation method thereof

(一)技术领域(1) Technical field

本发明涉及一种催化剂载体,特别涉及一种硅镁复合物载体及其制备方法。The invention relates to a catalyst carrier, in particular to a silicon-magnesium composite carrier and a preparation method thereof.

(二)背景技术(2) Background technology

催化剂载体又称担体(support),是负载型催化剂的组成之一。催化活性组分担载在载体表面上,载体主要用于支持活性组分,使催化剂具有特定的物理性状,而载体本身一般并不具有催化活性。多数载体是催化剂工业中的产品,常用的有氧化铝载体、硅胶载体、活性炭载体及某些天然产物如浮石、硅藻土等。目前,多采用压球法或挤条法制得载体母球,然后经活化焙烧和/或过热蒸汽扩孔处理获得最终的催化剂载体,这种工艺的缺点难以达到理想的细孔直径,比表面积和孔容积较小,从而造成载体的活性下降和交换容积降低,在催化合成产品时,就会影响单位体积的产量,并使载体的用量增加。The catalyst carrier, also known as the support, is one of the components of the supported catalyst. Catalytically active components are carried on the surface of the carrier, and the carrier is mainly used to support the active component to make the catalyst have specific physical properties, while the carrier itself generally does not have catalytic activity. Most carriers are products in the catalyst industry, commonly used are alumina carriers, silica gel carriers, activated carbon carriers, and some natural products such as pumice, diatomaceous earth, etc. At present, most of the carrier cue balls are prepared by pelletizing method or extruding method, and then the final catalyst carrier is obtained by activation roasting and/or superheated steam pore expansion treatment. The disadvantages of this process are that it is difficult to achieve the ideal pore diameter, specific surface area and The small pore volume will result in a decrease in the activity of the carrier and a decrease in the exchange volume, which will affect the output per unit volume and increase the amount of the carrier when catalyzing the synthesis of products.

(三)发明内容(3) Contents of the invention

本发明为了弥补现有技术的不足,提供了一种硅镁复合物载体及其制备方法。In order to make up for the deficiencies of the prior art, the invention provides a silicon-magnesium composite carrier and a preparation method thereof.

本发明是通过如下技术方案实现的:The present invention is achieved through the following technical solutions:

一种硅镁复合物载体,其特征在于:包括由硅、铝的氧化物和镁的碳酸盐及镁的氧化物组成的复合物,或由硅的氧化物和镁的碳酸盐及镁的氧化物组成的复合物为载体。A silicon-magnesium composite carrier, characterized in that: it includes a composite composed of silicon, aluminum oxide, magnesium carbonate, and magnesium oxide, or a silicon oxide, magnesium carbonate, and magnesium The composite composed of oxides is used as the carrier.

上述硅镁复合物载体的制备方法,包括以下步骤:The preparation method of above-mentioned silicon-magnesium composite carrier comprises the following steps:

(1)在烧杯中依次加入硅酸钠水溶液1000ml和20%氨水,通过20%氨水控制体系PH值为9-11,搅拌下升温至50-60℃;(1) Add 1000ml of sodium silicate aqueous solution and 20% ammonia water to the beaker in sequence, control the pH value of the system to 9-11 through 20% ammonia water, and raise the temperature to 50-60°C under stirring;

(2)在上述混合液中加入硝酸镁或硝酸镁和硝酸铝的混合溶液500ml混合均匀,搅拌1h后加入20%盐酸将体系pH值调整至4-6,再搅拌1h;(2) Add 500ml of magnesium nitrate or a mixed solution of magnesium nitrate and aluminum nitrate to the above mixture and mix evenly. After stirring for 1 hour, add 20% hydrochloric acid to adjust the pH value of the system to 4-6, and then stir for 1 hour;

(3)搅拌结束后,再向体系中加入2mol/L的碳酸铵溶液将体系pH值调整至8后,升温至80-90℃,搅拌6小时,然后老化40h得到沉淀物;(3) After the stirring is completed, add 2mol/L ammonium carbonate solution to the system to adjust the pH value of the system to 8, then raise the temperature to 80-90°C, stir for 6 hours, and then age for 40 hours to obtain the precipitate;

(4)将沉淀物过滤洗涤后于100-130℃下烘干,于400-600℃焙烧5小时,粉碎过200目筛,制得载体。(4) Filter and wash the precipitate, dry it at 100-130°C, bake it at 400-600°C for 5 hours, and crush it through a 200-mesh sieve to obtain the carrier.

上述硅酸钠水溶液浓度为:以二氧化硅计浓度为40-58克二氧化硅/升硅酸钠水溶液。The concentration of the above-mentioned sodium silicate aqueous solution is: calculated as silicon dioxide, the concentration is 40-58 grams of silicon dioxide per liter of sodium silicate aqueous solution.

上述步骤(2)中加入的硝酸镁的浓度为:以氧化镁计浓度为70-85克氧化镁/升硝酸镁。The concentration of the magnesium nitrate added in the above-mentioned step (2) is: in magnesium oxide, the concentration is 70-85 grams of magnesium oxide/liter of magnesium nitrate.

上述步骤(2)中加入的硝酸铝的浓度为:以氧化铝计浓度为50-100克氧化铝/升。The concentration of the aluminum nitrate added in the above step (2) is: calculated as alumina, the concentration is 50-100 grams of alumina/liter.

其中,所述载体孔容为0.6-1.5 ml/g,比表面积为55-130 m2/g。Wherein, the carrier has a pore volume of 0.6-1.5 ml/g and a specific surface area of 55-130 m 2 /g.

所述载体中硅、铝、镁的质量比例为,硅:铝:镁=5-7:0-3:2-5。The mass ratio of silicon, aluminum and magnesium in the carrier is silicon:aluminum:magnesium=5-7:0-3:2-5.

本发明的有益效果是:本发明提供了一种硅镁复合物载体,其中Si:Al:Mg=5-7:0-3:2-5;本发明制备方法简单,并且活性高,强度高,选择性好;并且本发明采用共沉淀法制得载体,增大了载体的比表面积和细孔容积。The beneficial effects of the present invention are: the present invention provides a silicon-magnesium composite carrier, wherein Si:Al:Mg=5-7:0-3:2-5; the preparation method of the present invention is simple, and has high activity and high strength , good selectivity; and the present invention adopts the co-precipitation method to prepare the carrier, which increases the specific surface area and pore volume of the carrier.

(四)具体实施方式(4) Specific implementation methods

实施例1:Example 1:

在一沉淀容器内依次加入以二氧化硅计浓度为44克二氧化硅/升的硅酸钠水溶液(水玻璃,以下同,青岛泡花碱厂产品)1000ml,以20%氨水(开元市化学试剂厂产品)控制体系pH值为10-11,搅拌下升温至60℃后,加入以氧化镁计浓度为71.3克氧化镁/升的硝酸镁(天津市耀华试剂厂产品)溶液250ml和以氧化铝计浓度为99.7克氧化铝/升的硝酸铝(沈阳市试剂一厂产品)溶液250ml混合液,在45-60℃下搅拌1小时后,使用20%盐酸再调整pH值为4-6,搅拌1小时,以2M的碳酸铵溶液调整pH值为8后,升温至80-90℃,再继续搅拌6小时,然后卸料,老化40小时,过滤洗涤,于125℃烘干。于550℃焙烧5小时后,经粉碎过200目筛,制得载体SAAdd 1000ml of sodium silicate aqueous solution (water glass, the same below, product of Qingdao Soda Soda Factory) with a concentration of 44 grams of silicon dioxide/liter in terms of silicon dioxide successively in a precipitation container, and add 1000ml of sodium silicate solution with 20% ammonia water (Kaiyuan Chemical Industry Co., Ltd.) Reagent factory product) to control the pH value of the system to 10-11, after stirring the temperature to 60°C, add 250ml of magnesium nitrate solution (product of Tianjin Yaohua Reagent Factory) and the following 250ml mixed solution of aluminum nitrate (product of Shenyang Reagent No. 1 Factory) solution with an alumina meter concentration of 99.7g/l, stirred at 45-60°C for 1 hour, then adjusted the pH value to 4-6 with 20% hydrochloric acid , stirred for 1 hour, adjusted the pH value to 8 with 2M ammonium carbonate solution, raised the temperature to 80-90°C, continued to stir for 6 hours, then unloaded, aged for 40 hours, filtered and washed, and dried at 125°C. After calcining at 550°C for 5 hours, the carrier S A was obtained by crushing and passing through a 200-mesh sieve.

实施例2:Example 2:

在一沉淀容器内依次加入以二氧化硅计浓度为50.6克二氧化硅/升的硅酸钠(青岛泡花碱厂产品)水溶液1000ml,以20%氨水(开元市化学试剂厂产品)控制体系pH值为10-11,搅拌下升温至60℃后,加入以氧化镁计浓度为80.7克氧化镁/升的硝酸镁(天津市耀华试剂厂产品)溶液250ml和以氧化铝计浓度为55.9克氧化铝/升硝酸铝(沈阳市试剂一厂产品)溶液250ml混合液,在45-60℃下搅拌1小时后,使用20%盐酸再调整pH值为4-6,搅拌1小时,以2M的碳酸铵溶液调整pH值为8后,升温至80-90℃,再继续搅拌6小时,然后卸料,老化40小时,过滤洗涤,于125℃烘干。于550℃焙烧5小时后,经粉碎过200目筛,制得载体SBAdd 1000ml of sodium silicate (product of Qingdao Soda Soda Factory) aqueous solution with a concentration of 50.6 grams of silicon dioxide per liter in a sedimentation container, and control the system with 20% ammonia water (product of Kaiyuan Chemical Reagent Factory). The pH value is 10-11. After heating up to 60°C under stirring, add 250ml of magnesium nitrate solution (product of Tianjin Yaohua Reagent Factory) with a concentration of 80.7 grams of magnesium oxide per liter as magnesium oxide and a solution of 55.9 grams of magnesium oxide as aluminum oxide. gram of alumina/liter of aluminum nitrate (product of Shenyang Reagent No. After adjusting the pH value of the ammonium carbonate solution to 8, the temperature was raised to 80-90°C, and the stirring was continued for 6 hours, then unloaded, aged for 40 hours, filtered and washed, and dried at 125°C. After calcining at 550°C for 5 hours, the carrier S B was obtained by crushing and passing through a 200-mesh sieve.

实施例3:Example 3:

在一沉淀容器内依次加入以氧化硅计浓度为55.2克氧化硅/升的硅酸钠(青岛泡花碱厂产品)水溶液1000ml,以20%氨水(开元市化学试剂厂产品)控制体系pH值为10-11,搅拌下升温至60℃后,加入以氧化镁计浓度为81.0克氧化镁/升的硝酸镁(天津市耀华试剂厂产品)溶液500ml,在45-60℃下搅拌1小时后,使用20%盐酸再调整pH值为4-6,搅拌1小时,以2M的碳酸铵溶液调整pH值为8后,升温至80-90℃,再继续搅拌6小时,然后卸料,老化40小时,过滤洗涤,于125℃烘干。于550℃焙烧5小时后,经粉碎过200目筛,制得载体SCAdd 1000ml of sodium silicate (product of Qingdao Soda Soda Factory) aqueous solution with a concentration of 55.2 grams of silicon oxide per liter in a sedimentation container in sequence, and control the pH value of the system with 20% ammonia water (product of Kaiyuan Chemical Reagent Factory) After heating to 60°C under stirring, add 500ml of magnesium nitrate solution (produced by Tianjin Yaohua Reagent Factory) with a concentration of 81.0 grams of magnesium oxide/liter in terms of magnesium oxide, and stir for 1 hour at 45-60°C Finally, use 20% hydrochloric acid to adjust the pH value to 4-6, stir for 1 hour, adjust the pH value to 8 with 2M ammonium carbonate solution, raise the temperature to 80-90°C, and continue stirring for 6 hours, then unload and age After 40 hours, filter and wash, and dry at 125°C. After calcining at 550° C for 5 hours, the carrier SC was obtained by crushing and passing through a 200-mesh sieve.

表1 本发明各实施例中载体的组分含量Table 1 The component content of the carrier in each embodiment of the present invention

Claims (5)

1.一种硅镁复合物载体,其特征在于:包括由硅、铝的氧化物和镁的碳酸盐及镁的氧化物组成的复合物,或由硅的氧化物和镁的碳酸盐及镁的氧化物组成的复合物为载体;所述载体孔容为0.6-1.5 ml/g,比表面积为55-130 m2/g;1. A silicon-magnesium composite carrier, characterized in that: comprise a compound composed of oxides of silicon, aluminum, carbonates of magnesium and magnesium, or by carbonates of oxides of silicon and magnesium The compound composed of magnesium oxide is the carrier; the pore volume of the carrier is 0.6-1.5 ml/g, and the specific surface area is 55-130 m 2 /g; 所述的硅镁复合物载体的制备方法,包括以下步骤:(1)在沉淀容器中依次加入硅酸钠水溶液1000ml和20%氨水,通过20%氨水控制体系pH值为9-11,搅拌下升温至50-60℃;(2)在上述混合液中加入硝酸镁或硝酸镁和硝酸铝的混合溶液500ml混合均匀,搅拌1h后加入20%盐酸将体系pH值调整至4-6,再搅拌1h;(3)搅拌结束后,再向体系中加入2mol/L的碳酸铵溶液将体系pH值调整至8后,升温至80-90℃,搅拌6小时,然后老化40h,得到沉淀物;(4)将沉淀物过滤洗涤后于100-130℃下烘干,于400-600℃焙烧5小时,粉碎过200目筛,制得载体。The preparation method of the silicon-magnesium composite carrier includes the following steps: (1) sequentially add 1000ml of sodium silicate aqueous solution and 20% ammonia water into the precipitation container, control the pH value of the system to 9-11 by 20% ammonia water, and stir Raise the temperature to 50-60°C; (2) Add 500ml of magnesium nitrate or a mixed solution of magnesium nitrate and aluminum nitrate to the above mixed solution and mix evenly. After stirring for 1 hour, add 20% hydrochloric acid to adjust the pH value of the system to 4-6, and then stir 1h; (3) After the stirring is completed, add 2mol/L ammonium carbonate solution to the system to adjust the pH value of the system to 8, then raise the temperature to 80-90°C, stir for 6 hours, and then age for 40h to obtain a precipitate; ( 4) Filter and wash the precipitate, dry it at 100-130°C, bake it at 400-600°C for 5 hours, and crush it through a 200-mesh sieve to obtain the carrier. 2.根据权利要求1所述的硅镁复合物载体,其特征在于:所述硅酸钠水溶液浓度为:以二氧化硅计浓度为40-58克二氧化硅/升硅酸钠水溶液。2. The silicon-magnesium composite carrier according to claim 1, characterized in that: the concentration of the sodium silicate aqueous solution is: calculated as silicon dioxide, the concentration is 40-58 grams of silicon dioxide per liter of sodium silicate aqueous solution. 3.根据权利要求1所述的硅镁复合物载体,其特征在于:所述步骤(2)中加入的硝酸镁的浓度为:以氧化镁计浓度为70-85克氧化镁/升硝酸镁。3. The silicon-magnesium composite carrier according to claim 1, characterized in that: the concentration of magnesium nitrate added in the step (2) is: calculated as magnesium oxide, the concentration is 70-85 grams of magnesium oxide/liter of magnesium nitrate . 4.根据权利要求1所述的硅镁复合物载体,其特征在于:所述步骤(2)中加入的硝酸铝的浓度为:以氧化铝计浓度为50-100克氧化铝/升。4. The silicon-magnesium composite carrier according to claim 1, characterized in that: the concentration of aluminum nitrate added in the step (2) is: calculated as alumina, the concentration is 50-100 g alumina/liter. 5.根据权利要求1所述的硅镁复合物载体,其特征在于:所述载体中硅、铝、镁的质量比为,硅:铝:镁=5-7:0-3:2-5。5. The silicon-magnesium composite carrier according to claim 1, characterized in that: the mass ratio of silicon, aluminum, and magnesium in the carrier is, silicon:aluminum:magnesium=5-7:0-3:2-5 .
CN201510258411.5A 2015-05-20 2015-05-20 A kind of silicon magnesium complexes carrier and preparation method thereof Active CN104888866B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510258411.5A CN104888866B (en) 2015-05-20 2015-05-20 A kind of silicon magnesium complexes carrier and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510258411.5A CN104888866B (en) 2015-05-20 2015-05-20 A kind of silicon magnesium complexes carrier and preparation method thereof

Publications (2)

Publication Number Publication Date
CN104888866A CN104888866A (en) 2015-09-09
CN104888866B true CN104888866B (en) 2017-06-16

Family

ID=54022069

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510258411.5A Active CN104888866B (en) 2015-05-20 2015-05-20 A kind of silicon magnesium complexes carrier and preparation method thereof

Country Status (1)

Country Link
CN (1) CN104888866B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114539598A (en) * 2022-03-24 2022-05-27 慈溪市赞恩包装科技有限公司 Preparation method of foam board with uniform particles

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1422198A1 (en) * 2001-07-27 2004-05-26 Chiyoda Corporation Porous 4 group metal oxide and method for preparation thereof
CN1907567A (en) * 2006-08-16 2007-02-07 天津化工研究设计院 Forming method for porous composite metallic oxide catalytic carrier
CN101613110A (en) * 2008-12-16 2009-12-30 海南美大制药有限公司 A kind of aluminum-magnesium silicate compound and synthetic method thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1422198A1 (en) * 2001-07-27 2004-05-26 Chiyoda Corporation Porous 4 group metal oxide and method for preparation thereof
CN1907567A (en) * 2006-08-16 2007-02-07 天津化工研究设计院 Forming method for porous composite metallic oxide catalytic carrier
CN101613110A (en) * 2008-12-16 2009-12-30 海南美大制药有限公司 A kind of aluminum-magnesium silicate compound and synthetic method thereof

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
共沉淀法合成三硅酸镁及其微观分析;冯凌等;《北京科技大学学报》;20091231;第31卷(第2期);第1.1节 *

Also Published As

Publication number Publication date
CN104888866A (en) 2015-09-09

Similar Documents

Publication Publication Date Title
CN101648134B (en) Copper-silicon catalyst for preparing ethylene glycol by dimethyl oxalate hydrogenation and preparation method thereof
CN105478161A (en) Selective catalytic reduction(SCR)denitration catalyst based on titanium slag and preparation method thereof
CN108993576A (en) A kind of zinc catalyst and preparation method thereof for catalyzing acetylene hydration reaction
WO2018233497A1 (en) Copper-based catalyst and preparation method therefor, and method for preparing etherification-grade ethylene glycol by using catalyst
CN102259900A (en) Hydrated alumina and preparation method thereof
CN112794351B (en) A kind of preparation method of macroporous activated alumina powder
CN108722408A (en) A kind of catalyst and preparation method thereof of dimethyl oxalate gas phase hydrogenation synthesizing glycol
CN103012114B (en) Method of synchronously preparing DL-tartaric acid and DL-potassium hydrogen tartrate
CN105854859A (en) Efficient bifunctional catalyst as well as preparation and application thereof
CN104888866B (en) A kind of silicon magnesium complexes carrier and preparation method thereof
CN1251801C (en) Preparing method for catalyst with macroporous silica gel as carrier
CN118022701B (en) Small pore size silica gel clarifier and preparation method and application thereof
CN103739479B (en) Method for preparing sodium gluconate through catalytic oxidation of glucose by using gold catalyst
CN1325375C (en) Beta zeolite granule possessing multiple grade pore passage and its preparation method
CN106673032A (en) High-acidity low-crystallinity alumina dry glue and preparation method thereof
CN104667904B (en) The preparation method of fructose
CN109499582B (en) Composite oxide mimic enzyme material and preparation method and application thereof
CN105712370A (en) USY molecular sieve with double meso-structures and preparation method thereof
CN102000611A (en) Catalyst for synthesizing tirbutyl citrate and preparation method thereof
CN104475147B (en) A nanometer ZSM-5/γ-Al2O3 composite catalyst for glycerin dehydration to acrolein, its preparation method and application
CN103464192A (en) Mesoporous nickel-molybdenum oxide catalyst, and preparation method and application thereof
CN103316677B (en) A kind of catalyst for sec-butyl alcohol dehydrogenizing and preparation method
CN105314652B (en) A kind of preparation method of the molecular sieves of H types ZSM 5
CN105907828B (en) A kind of substrate processing method for the reaction of phytosterol Side chain cleavage
CN105688877A (en) Fischer-Tropsch synthesis iron-based catalyst and preparation method thereof

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
TR01 Transfer of patent right

Effective date of registration: 20211201

Address after: 274000 west of north section of Huaxu road and north of Changcheng street, ChenWang sub district office, juancheng County, Heze City, Shandong Province

Patentee after: JUANCHENG DINGSHENG CHEMICAL TECHNOLOGY Co.,Ltd.

Address before: 274600 east of Fenghuang Road south of Chengpu Street juancheng County Heze City Shandong Province

Patentee before: JUANCHENG RUIDING TECHNOLOGY Co.,Ltd.

TR01 Transfer of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: Silicon magnesium composite carrier and preparation method thereof

Effective date of registration: 20211221

Granted publication date: 20170616

Pledgee: Shandong juancheng Rural Commercial Bank Co.,Ltd.

Pledgor: JUANCHENG DINGSHENG CHEMICAL TECHNOLOGY Co.,Ltd.

Registration number: Y2021980015438

PE01 Entry into force of the registration of the contract for pledge of patent right
PC01 Cancellation of the registration of the contract for pledge of patent right

Granted publication date: 20170616

Pledgee: Shandong juancheng Rural Commercial Bank Co.,Ltd.

Pledgor: JUANCHENG DINGSHENG CHEMICAL TECHNOLOGY Co.,Ltd.

Registration number: Y2021980015438

PC01 Cancellation of the registration of the contract for pledge of patent right