in:(Liquan Li)
LAYERED OXIDE MATERIAL CONTAINING COPPER, AND PREPARATION METHOD AND USE THEREOF
PCT/CN2015/081802
[HU, Yongsheng 胡勇胜, HU, Yongsheng 胡勇胜, LI, Yunming 李云明, HU, Yongsheng 胡勇胜, LI, Yunming 李云明, XU, Shuyin 徐淑银, HU, Yongsheng 胡勇胜, LI, Yunming 李云明, XU, Shuyin 徐淑银, WANG, Yuesheng 王跃生, HU, Yongsheng 胡勇胜, LI, Yunming 李云明, XU, Shuyin 徐淑银, WANG, Yuesheng 王跃生, CHEN, Liquan 陈立泉, HU, Yongsheng 胡勇胜, LI, Yunming 李云明, XU, Shuyin 徐淑银, WANG, Yuesheng 王跃生, CHEN, Liquan 陈立泉, HUANG, Xuejie 黄学杰]
No. 8, 3rd South Street 中国北京市海淀区中关村南三街8号, Beijing 100190Zhongguancun, Haidian DistrictBeijing 100190
Disclosed are a layered oxide material containing copper, and a preparation method and the use thereof. The material has the general chemical formula of Na0.68+aNibCucMdMneO2+δ, wherein Ni, Cu, M and Mn respectively form an octahedral structure with six nearest-neighbour oxygen atoms and form transition metal layers through an edge-shared arrangement; alkali metal ions Na+ are located between every two layers of transition metal layers; M is specifically one or more of Mg2+, Mn2+, Zn2+, Co2+, Al3+, B3+, Cr3+, Mn3+, Co3+, V3+, Zr4+, Ti4+, Sn4+, Mo4+, Ru4+, Nb4+, Sb5+, Nb5+, Mo6+ and Te6+; and a, b, c, d, e, δ and m satisfy (0.68 + a) + 2(b + c) + md + 4e = 2(2 + δ) and b + c + d + e = 1.
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PIN STRUCTURE, METHOD FOR OPERATING THE SAME, AND SUPPORTING DEVICE CONTAINING THE SAME
PCT/CN2016/082887
[HUANG, Yang, HUANG, Yang, CUI, Liquan, HUANG, Yang, CUI, Liquan, LI, Lin]
No.10 Jiuxianqiao Rd., Chaoyang District,Beijing 100015;No. 118 Jinghaiyilu, BDA,Beijing 100176
The present disclosure provides a pin structure for providing support to a substrate. The pin structure includes a first supporting unit and a second supporting unit over the first supporting unit. The first supporting unit includes at least one first supporting pin, each supporting pin being insertable through a pin hole of a lower panel; and the second supporting unit includes at least two second supporting pins for supporting a substrate.
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LIQUID METAL CATHODE MATERIAL AND ROOM-TEMPERATURE LIQUID METAL BATTERY, AND PREPARATION METHOD THEREOF AND USAGE THEREOF
PCT/CN2015/081807
[HU, Yongsheng 胡勇胜, HU, Yongsheng 胡勇胜, YU, Juezhi 余觉知, HU, Yongsheng 胡勇胜, YU, Juezhi 余觉知, CHU, Geng 褚赓, HU, Yongsheng 胡勇胜, YU, Juezhi 余觉知, CHU, Geng 褚赓, LI, Hong 李泓, HU, Yongsheng 胡勇胜, YU, Juezhi 余觉知, CHU, Geng 褚赓, LI, Hong 李泓, HUANG, Xuejie 黄学杰, HU, Yongsheng 胡勇胜, YU, Juezhi 余觉知, CHU, Geng 褚赓, LI, Hong 李泓, HUANG, Xuejie 黄学杰, CHEN, Liquan 陈立泉]
No.8, 3rd South Street, Zhongguancun, Haidian District 中国北京市海淀区中关村南三街8号, Beijing 100190Beijing 100190
Disclosed are a liquid metal cathode material and a room-temperature liquid metal battery, and a preparation method therefor and usage thereof. The cathode material is dark green liquid generated by mixing alkali metal, an aromatic compound and an ether solvent. The alkali metal is any one of metallic sodium, metallic lithium or metallic potassium. The aromatic compound is any one of biphenyl, derivatives of biphenyl, naphthaline, derivatives of naphthaline, anthracene or derivatives of the anthracene. The ether solvent comprises one or more of glycol dimethyl ether, diethylene glycol dimethyl ether or tetraethylene glycol dimethyl ether, etc.
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METHOD FOR PREPARING FUEL FROM BIOMASS PYROLYSIS LIQUID
PCT/CN2020/083643
[YUAN, Yuanping 袁远平, LI, Liquan 李立权, WANG, Hualin 汪华林, CHEN, Chonggang 陈崇刚, LI, Jianping 李剑平, ZHAO, Ying 赵颖, YANG, Xuejing 杨雪晶, LI, Junjie 李俊杰, CHAO, Junrui 晁君瑞, ZHENG, Xuhui 郑旭晖]
No. 219 Jinshui Road 中国河南省郑州市金水路219号, Henan 450000Zhengzhou, Henan 450000;No. 27 Zhongzhou West Road 中国河南省洛阳市中州西路27号, Henan 471003Luoyang, Henan 471003;No. 19, Lane 188, Maoting Road, Songjiang Industrial Zone 中国上海市松江工业区泖亭路188弄财富兴园19栋, Shanghai 201611Shanghai 201611
Disclosed is a method for preparing fuel from a biomass pyrolysis liquid. A biomass pyrolysis liquid that is not pretreated is added to a reaction zone of a fluidized bed reactor under the protection of a hydrogen donor to perform hydrotreatment. The biomass pyrolysis liquid is hydrogenated and converted into fuel in the fluidized bed reactor in which a full mixing and fluidifying catalyst circulating system formed by the combined action of circulating oil, catalyst, hydrogen, and internal components. Part of the fuel is returned to the fluidized bed reactor as circulating oil, and the other part is discharged as a product. The fuel obtained by the present invention is miscible with fossil fuel by any ratio, has a very low sulfur and nitrogen content, and contains a certain proportion of oxygen to facilitate complete combustion, especially in high altitude areas. In addition, the present invention prevents the condensation and coking of biomass pyrolysis liquid against heating, so that the problem of fast deactivation of catalyst is solved, the formation of coke is prevented, and the requirements of industrialized long-period operation can be satisfied. Disclosed is a method for preparing fuel from a biomass pyrolysis liquid. A biomass pyrolysis liquid that is not pretreated is added to a reaction zone of a fluidized bed reactor under the protection of a hydrogen donor to perform hydrotreatment. The biomass pyrolysis liquid is hydrogenated and converted into fuel in the fluidized bed reactor in which a full mixing and fluidifying catalyst circulating system formed by the combined action of circulating oil, catalyst, hydrogen, and internal components. Part of the fuel is returned to the fluidized bed reactor as circulating oil, and the other part is discharged as a product. The fuel obtained by the present invention is miscible with fossil fuel by any ratio, has a very low sulfur and nitrogen content, and contains a certain proportion of oxygen to facilitate complete combustion, especially in high altitude areas. In addition, the present invention prevents the condensation and coking of biomass pyrolysis liquid against heating, so that the problem of fast deactivation of catalyst is solved, the formation of coke is prevented, and the requirements of industrialized long-period operation can be satisfied.
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METHOD FOR PREPARING HIGH-QUALITY FUEL OIL AND/OR CHEMICAL RAW MATERIAL FROM BIOMASS PYROLYSIS LIQUID
PCT/CN2020/083642
[LI, Liquan 李立权, WANG, Hualin 汪华林, YUAN, Yuanping 袁远平, CHEN, Chonggang 陈崇刚, LI, Jianping 李剑平, ZHAO, Ying 赵颖, YANG, Xuejing 杨雪晶, LI, Junjie 李俊杰, CHAO, Junrui 晁君瑞, ZHENG, Xuhui 郑旭晖]
No. 219 Jinshui Road 中国河南省郑州市金水路219号, Henan 450000Zhengzhou, Henan 450000;No. 27 Zhongzhou West Road 中国河南省洛阳市中州西路27号, Henan 471003Luoyang, Henan 471003;No. 19, Lane 188, Maoting Road 中国上海市松江工业区泖亭路188弄财富兴园19栋, Shanghai 201611Songjing Industrial ZoneShanghai 201611
Disclosed by the present invention is a method for preparing a high-quality fuel oil and/or chemical raw material from a biomass pyrolysis liquid. In the method, a biomass pyrolysis liquid undergoes a hydrodeoxygenation reaction in a catalyst full mixing flow circulation system in a fluidized bed reactor to obtain deoxygenated oil, and the obtained deoxygenated oil undergoes a hydrocracking reaction in a fixed bed reactor to obtain high-quality fuel oil and/or a chemical raw material. The method of the present invention may prevent the condensation and coking of a biomass pyrolysis liquid, solve the problem of rapid catalyst deactivation, and may convert a biomass pyrolysis liquid into a high-quality fuel oil that may be directly used by vehicles and into a chemical product.
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METHOD FOR PREPARING HIGH-QUALITY FUEL OIL AND/OR CHEMICAL RAW MATERIAL FROM BIOMASS PYROLYSIS LIQUID
US17606481
[Liquan LI, Hualin WANG, Yuanping YUAN, Chonggang CHEN, Jianping LI, Ying ZHAO, Xuejing YANG, Junjie LI, Junrui CHAO, Xuhui ZHENG]
CN Zhengzhou
A method for preparing a high-quality fuel oil and/or chemical raw material from a biomass pyrolysis liquid. In the method, a biomass pyrolysis liquid undergoes a hydrodeoxygenation reaction in a catalyst full mixing flow circulation system in a fluidized bed reactor to obtain deoxygenated oil, and the obtained deoxygenated oil undergoes a hydrocracking reaction in a fixed bed reactor to obtain high-quality fuel oil and/or a chemical raw material. The method may prevent the condensation and coking of a biomass pyrolysis liquid, solve the problem of rapid catalyst deactivation, and may convert a biomass pyrolysis liquid into a high-quality fuel oil that may be directly used by vehicles and into a chemical product.
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EXCAVATION TUNNEL FULL-WAVEFORM INVERSION METHOD BASED ON MULTI-PARAMETER CONSTRAINT AND STRUCTURE CORRECTION
PCT/CN2023/113748
[LI, Shenglin 李圣林, ZHANG, Pingsong 张平松, LI, Jie 李洁, GUO, Liquan 郭立全, QIU, Shi 邱实]
{No.168, Taifeng Street 中国安徽省淮南市泰丰大街168号, Anhui 232001Huainan, Anhui 232001;CN CN(CN)(CN)}
Disclosed in the present invention is an excavation tunnel full-waveform inversion method based on multi-parameter constraint and structure correction. The method comprises the following steps: step 1, constructing a full-waveform inversion initial model, and then performing single-scale inversion on the initial model by using a multi-scale elastic-wave full-waveform inversion method; step 2, performing multi-parameter weighted constraint and structure correction on the single-scale inversion result, so as to obtain a preliminary correction result; step 3, on the basis of a preset limiting condition, performing one-dimensional wave-velocity profile space structure correction and smooth constraint on the preliminary correction result, so as to obtain a secondary correction result; step 4, using the secondary correction result as an initial model of the next scale, and continuing to perform full-waveform inversion; and repeating steps 2-4 until the inversion of all the scales is completed, so as to obtain a full-waveform inversion result. The present invention can effectively solve the problems of the observation system being highly restricted, the detection data volume being relatively small, the offset distance being relatively small, and the multiplicity of solution of waveform inversion being high in terms of advanced detection of an excavation tunnel, thus improving the inversion effect.
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PYROLYTIC AMORPHOUS CARBON MATERIAL, PREPARATION METHOD AND USE THEREOF
PCT/CN2015/081841
[HU, Yongsheng 胡勇胜, HU, Yongsheng 胡勇胜, LI, Yunming 李云明, HU, Yongsheng 胡勇胜, LI, Yunming 李云明, CHEN, Liquan 陈立泉]
No.8, 3rd South Street, Zhongguancun, Haidian District 中国北京市海淀区中关村南三街8号, Beijing 100190Beijing 100190
A pyrolytic amorphous carbon material, preparation method and the use thereof. The pyrolytic amorphous carbon material is in the shape of a particle having an average diameter of 1-100μm, a d 002 value between 0.35 and 0.44nm, an L c value between 0.5 and 4nm, and an L 8 value between 3 and 5nm. The preparation method thereof comprises: adding a hard carbon precursor and a soft carbon precursor to a solvent and uniformly mixing the same to obtain a slurry; drying and then cross-linking the slurry in an inert atmosphere at 200-600℃, curing for 0.5-5 hours; treating the slurry in the inert atmosphere at a high temperature of 1000-1600℃ for 0.5-10 hours ; and after cooling, obtaining the pyrolytic amorphous carbon material. The material has broad use, and is especially suitable to be used as negative electrode material of sodium ion secondary battery or lithium ion secondary battery.
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PROCESS AND DEVICE FOR TREATING CATALYST DISCHARGED FROM BUBBLING BED HYDROGENATION OF RESIDUAL OIL
CA2872696A
[LI JIANPING, WANG JIANGANG, WANG HUALIN, ZHANG YANHONG, CUI XIN, SHEN LING, LI LIQUAN, CHEN CHONGGANG, ZENG QIAN, ZHAO YING]
CN
The invention relates to a process and a device for treating a catalyst discharged from bubbling bed hydrogenation of residual oil. Provided is a process for treating a catalyst discharged from bubbling bed hydrogenation of residual oil, comprising the following steps: (1) adjustment and control to reduce the viscosity, wherein the catalyst discharged intermittently from a bubbling bed hydrogenation reactor for the residual oil is adjusted for storage and then discharged continuously, subjected to temperature adjustment by adding water, such that the viscosity of the oil adsorbed on the surfaces and inside the pores of the discharged catalyst particles is reduced, and the flowability of the adsorbed oil on the surfaces and inside the pores of the discharged catalyst particles is improved; (2) desorption and separation by rotational flow, wherein the adsorbed oil is desorbed and separated from the surfaces and inner pores of the discharged catalyst particles by a flowing shear force in a rotational flow field; and (3) separation and resource utilization of the three phase oil-water-catalyst, wherein the oil/water/catalyst mixture produced from the desorption and separation by rotational flow is subjected to three-phase separation, achieving recovery of the oil, recycling of the water obtained by separation, and full recovery of the solid particles obtained by separation. Also provided is a device for treating a catalyst discharged from bubbling bed hydrogenation of residual oil.
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PROCESS AND DEVICE FOR TREATING CATALYST DISCHARGED FROM HYDROGENATION OF BUBBLING BED RESIDUAL OIL
IN10200DEN2014A
[LI JIANPING, WANG JIANGANG, WANG HUALIN, ZHANG YANHONG, CUI XIN, SHEN LING, LI LIQUAN, CHEN CHONGGANG, ZENG QIAN, ZHAO YING]
CN
Provided is a process for treating a catalyst discharged from the hydrogenation of a bubbling bed residual oil the method comprising the following steps: (1) adjustment and control to reduce the viscosity wherein the catalyst discharged intermittently from a reactor for the hydrogenation of a bubbling bed residual oil is adjusted for storage and then discharged continuously subjected to temperature adjustment by adding water such that the viscosity of the oil adsorbed on the surfaces and inside the pores of the discharged catalyst particles is reduced and the flowability of the oil adsorbed on the surfaces and inside the pores of the discharged catalyst particles is improved; (2) desorption and separation by rotational flow wherein the adsorbed oil is desorbed and separated from the surfaces and the inside pores of the discharged catalyst particles by a flowing shear force from a rotational flow field; and (3) separation and resource utilization of the three phase oil water catalyst wherein the oil/water/catalyst mixture produced from the desorption and separation by rotational flow is subjected to a three phase separation achieving the recovery of the oil the recycling of the water obtained by separation and full recovery of the solid particles obtained by separation. Also provided is a device for treating a catalyst discharged from the hydrogenation of a bubbling bed residual oil and the use of this device in the treatment of oil containing solid waste.
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