WO1996033949A1 - Procede et dispositif de production de graphite oxyde - Google Patents
Procede et dispositif de production de graphite oxyde Download PDFInfo
- Publication number
- WO1996033949A1 WO1996033949A1 PCT/RU1996/000106 RU9600106W WO9633949A1 WO 1996033949 A1 WO1996033949 A1 WO 1996033949A1 RU 9600106 W RU9600106 W RU 9600106W WO 9633949 A1 WO9633949 A1 WO 9633949A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- group
- gρaφiτa
- acid
- graphite
- anode
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/20—Graphite
- C01B32/21—After-treatment
- C01B32/23—Oxidation
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/20—Graphite
- C01B32/21—After-treatment
- C01B32/22—Intercalation
- C01B32/225—Expansion; Exfoliation
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/11—Powder tap density
Definitions
- the regulator when processing a gray acid charge, the regulator is also regulated by a combination of oxidizing agents.
- the introduction of the necessary fuming ⁇ 0 3 add ⁇ 2 0 5 ( ⁇ Economics ⁇ ⁇ ., ⁇ . ⁇ gd. ⁇ d.Set., 1938, ⁇ 238, ⁇ 1, 5.1 -50; ⁇ . ⁇ réelle * ⁇ réelle ⁇ ⁇ . ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ ... ⁇ ⁇ ⁇ ⁇ , 22 ⁇ 2, ⁇ . 131 -133, 1984; ⁇ . ⁇ . ⁇ Indian ⁇ réelle ⁇ Certainly ⁇ . Cactus, 30 ⁇ 6, pp. 819-823, 1992).
- Foam - extremely light chemically inert carbon material with a developed specific turnaround and good dehumidifying, non-corrosive and non-corrosive materials. Foam is easy to press into a flexible group foil. Products on its basis find a wide range of applications, including storage, packing, rings, antiques and t. ⁇ . (Pat. F. Stations ⁇ 1395964, ⁇ 04 ⁇ 35/54, 1965; Pat. ⁇ ⁇ 4102960, ⁇ 04 ⁇ 35/52, 1978).
- the method of receipt of an acidified group is known, which is included in the processing of a group of a quick acid with an addition of 2-5 parts by weight. water soda per 100 parts by weight ⁇ 2 50 4 .
- the process needs to be used 80-90% ⁇ 2 0 2 (United States ⁇ 4091083, ⁇ 01 ⁇ 31/04, 1978).
- the aforementioned method is purely environmentally friendly, the only use of which is a high concentration of processed water results in a loss of health.
- Wastewater is a large profit of an oxidizing agent, and it is also not necessary to use a medium acid solution of 98%.
- Serious acid is not disposed of.
- the density of the flow is 40–50 m ⁇ / cm 2 , the voltage increases in the process of processing from 2.3 to 4.4 ⁇ .
- Received a further processing charge has a bulk density of 0.004 g / cm 3 .
- the method is cyclic and inefficient due to the large process: the process is carried out for 7 hours.
- ⁇ ed ⁇ s ⁇ a ⁇ m s ⁇ s ⁇ ba yavlyae ⁇ sya ⁇ a ⁇ zhe ⁇ vedenie ele ⁇ imiches ⁇ g ⁇ ⁇ isleniya g ⁇ a ⁇ i ⁇ a ⁇ i ⁇ s ⁇ yann ⁇ y ⁇ l ⁇ n ⁇ s ⁇ i ⁇ a, ch ⁇ not ⁇ zv ⁇ lyae ⁇ ⁇ lucha ⁇ ⁇ dn ⁇ dny ⁇ du ⁇ ⁇ i is ⁇ lz ⁇ vanii b ⁇ lsh ⁇ g ⁇ ⁇ liches ⁇ va g ⁇ a ⁇ i ⁇ a.
- the oxidized group is produced with a bulk density of 0.012 g / cm 3 (Patent ⁇ ⁇ 4244934, ⁇ 01 1981. Unequivocally used is an unacceptable oxidizer that makes the process uneconomical. At the same time, the oxidized group has a low degree of expansion.
- the proposed method makes it possible to enjoy a high share of the product in an oxidized manner with a high rate of loss. To ensure that the equipment is available in the factory, the equipment is also available as an option.
- the indicated range of potentials ensures the receipt of a single, acidified unit with an adjustable degree of expansion.
- a decrease in potentials below the indicated values results in the increase of only the highest degrees of compounds of incorporation into the group with a low degree of expansion.
- Boosting Potentially Unskilled Engineers, t. ⁇ . Reduces oxidation of the graphite and reduces the degree of its expansion.
- the degree of expansion of the acidified load depends on the number of degrees of integration of the installation: the lower the speed is, the larger the more Therefore, the redundancy of the group should be subject to the directly controlled conditions that ensure the connection of the connected connection.
- One of the basic factors that determine the synthesis of a given degree is the potential value, and the value 6 The machine is being processed.
- the equal values of the analogous potentials necessary for the synthesis of I – III degrees are 0.46–0.55 ⁇ for the III stage, 0.55–0.83 ⁇ for the II stage and above 0.83 ⁇ for the I connection ) group.
- the oxidizing potential of the oxidizing agent in the sulfuric acid industry is dependent on the oxidizing agent and the sulfuric acid concentration.
- E ⁇ s ⁇ e ⁇ imen ⁇ aln ⁇ us ⁇ an ⁇ vlen ⁇ if the value ch ⁇ ⁇ ed ⁇ s- ⁇ entsiala ⁇ isli ⁇ elya in ⁇ as ⁇ v ⁇ e se ⁇ n ⁇ y ⁇ isl ⁇ y s ⁇ v ⁇ adae ⁇ with ele ⁇ imiches ⁇ imi ⁇ entsialami ⁇ b ⁇ az ⁇ vaniya I s ⁇ u ⁇ eni, ⁇ in ⁇ ezul ⁇ a ⁇ e ⁇ imiches ⁇ g ⁇ sin ⁇ eza bude ⁇ ⁇ luchena I s ⁇ u ⁇ en bisul ⁇ a ⁇ a g ⁇ a ⁇ i ⁇ a.
- the diaphragm is made in the form of a ring with pores for the blades;
- the appliance is made in the form of a wheel with rotors for the blades secured on the sowing shaft.
- the unit has a user interface and is installed in the lower part of the compartment between the loading and unloading units.
- the negative shaft is displaced by the negative output shaft with an increase in the gap between the anode and the inlet at 1, 5-3 of the inlet of the outlet ⁇ me ⁇ g ⁇ , us ⁇ ys ⁇ v ⁇ m ⁇ zhe ⁇ by ⁇ snabzhen ⁇ smesi ⁇ elem with ⁇ a ⁇ ub ⁇ ami for ⁇ dachi ⁇ eagen ⁇ v and inzhe ⁇ m for ⁇ dachi gaz ⁇ b ⁇ azny ⁇ ⁇ isli ⁇ eley and ⁇ a ⁇ ub ⁇ m Removal ⁇ dyaschi ⁇ gaz ⁇ v and ⁇ a ⁇ ub ⁇ ami Removal ⁇ b ⁇ az ⁇ vavshi ⁇ sya ⁇ du ⁇ v, ⁇ din of ⁇ y ⁇ ⁇ ds ⁇ edinen ⁇ zag ⁇ uz ⁇ chn ⁇ mu ⁇ a ⁇ ub ⁇ u ⁇ ea ⁇ a che ⁇ ez ⁇ i ⁇ a ⁇ el.
- Fig. 1 a cross-section of the process, which is a part of the device for receiving an acidified product, is provided.
- Fig. 2 it is a device for receiving an oxidized unit with a mixer and a unit for chemical processing of a unit.
- the unit is equipped with a cylinder 1 with a cylindrical internal unit with units 2 and 3, which is suitable for downloading unused reagents and unloading units.
- a cylinder 1 with a cylindrical internal unit with units 2 and 3, which is suitable for downloading unused reagents and unloading units.
- anode 4 is installed, made in the form of a ring.
- ⁇ ezhdu ⁇ ve ⁇ n ⁇ s ⁇ yu an ⁇ da 4 ⁇ ltsev ⁇ y dia ⁇ agm ⁇ y 8 and two adjacent l ⁇ a ⁇ ami 6 ⁇ b ⁇ az ⁇ vany isolated areas 9 for electrical processing.
- ⁇ of the lower part of the housing 1 has been installed a tertiary-selective elec- trode of comparison 10 for measuring the analogous potential of the elec- trical process.
- the anode 4 is offset by a positive shaft 5, so the gap between the 8th and the 4th anode extends to 1,5-3 times the download area is out of sight.
- the unit is 4;
- Bulk version ⁇ 2 50 4 : group 1, 2.
- Advance movement of the patient 6 adjusts to a 19 ⁇ z ⁇ ne vyg ⁇ uz ⁇ i l ⁇ a ⁇ i 6 u ⁇ a ⁇ livalis and bisul ⁇ a ⁇ g ⁇ a ⁇ i ⁇ a scraping with ⁇ ve ⁇ n ⁇ s ⁇ i dia ⁇ agmy 8.
- ⁇ a vy ⁇ dn ⁇ m ⁇ a ⁇ ub ⁇ e 3 che ⁇ ez 1, 5 chasa ⁇ is ⁇ dila ne ⁇ e ⁇ yvnaya vyg ⁇ uz ⁇ a ⁇ du ⁇ a as gus ⁇ y ⁇ ul ⁇ y bisul ⁇ a ⁇ a g ⁇ a ⁇ i ⁇ a in se ⁇ n ⁇ y ⁇ isl ⁇ e.
- 10 ⁇ mixer 11 was loaded with 20 kg of bulk and 24 l of sulfuric acid
- the variation in density did not exceed 3%.
- Foam content ⁇ 0, 1 wt.%.
- the degree of expansion of the oxidized group was 600 cm 3 / g.
- the load they turned on the agitator at a speed of 30 rpm and turned on the oxidizing process at a speed of only 2 50 4 :
- the mixture was supplied through the unit 17 and the screw unit 18 into the unloading unit 2 of the process unit for the supply of electrical equipment.
- the mixture was fed to the reactor with a waste of 6 kg / hour for the unit.
- a cylindrical mixer 1 equipped with a stirrer (not shown), through the appliance 12 with a charge of 15%, an unloading unit of 250 Then they turned on the agitator at a speed of 30 rpm and through the unit fifteen
- the invention may be used to receive a charge in a variety of areas.
- the synthesis of intrusion into a unit with the following hydraulic system is the first stage of the receipt of a unit.
- ⁇ a ⁇ e ⁇ ial on ⁇ sn ⁇ ve ⁇ en ⁇ g ⁇ a ⁇ i ⁇ a is ⁇ lzue ⁇ sya in mashin ⁇ s ⁇ enii, ⁇ imiches ⁇ y, a ⁇ mn ⁇ y, ae ⁇ smiches ⁇ y ⁇ myshlenn ⁇ s ⁇ i, ⁇ e ⁇ l ⁇ e ⁇ ni ⁇ e and d ⁇ ugi ⁇ ⁇ aslya ⁇ ⁇ myshlenn ⁇ s ⁇ i in ⁇ aches ⁇ ve zaschi ⁇ ny ⁇ ⁇ y ⁇ y, ⁇ lad ⁇ and u ⁇ l ⁇ neny, ⁇ ab ⁇ ayuschi ⁇ i ⁇ vyshenny ⁇ em ⁇ e ⁇ a ⁇ u ⁇ a ⁇ ius ⁇ ychivy ⁇ ⁇ deys ⁇ viyu ⁇ imiches ⁇ i ⁇ ⁇
- the proposed invention provides for the production of a single unit of an oxidized unit with a high specific output of the process.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Carbon And Carbon Compounds (AREA)
- Nitrogen And Oxygen Or Sulfur-Condensed Heterocyclic Ring Systems (AREA)
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE69606529T DE69606529T2 (de) | 1995-04-28 | 1996-04-26 | Verfahren und vorrichtung zur herstellung von oxidiertem graphit |
EP96915254A EP0823398B1 (en) | 1995-04-28 | 1996-04-26 | Process and device for obtaining oxidised graphite |
Applications Claiming Priority (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
RU95106784 | 1995-04-28 | ||
RU95106784/25A RU95106784A (ru) | 1995-04-28 | 1995-04-28 | Способ получения бисульфата графита и реактор для его осуществления |
RU96103543 | 1996-02-22 | ||
RU96103479 | 1996-02-22 | ||
RU96103479A RU2090498C1 (ru) | 1996-02-22 | 1996-02-22 | Способ получения окисленного графита |
RU96103543A RU2089495C1 (ru) | 1996-02-22 | 1996-02-22 | Способ получения окисленного графита |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1996033949A1 true WO1996033949A1 (fr) | 1996-10-31 |
Family
ID=27354153
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/RU1996/000106 WO1996033949A1 (fr) | 1995-04-28 | 1996-04-26 | Procede et dispositif de production de graphite oxyde |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP0823398B1 (ru) |
CN (1) | CN1074747C (ru) |
DE (1) | DE69606529T2 (ru) |
WO (1) | WO1996033949A1 (ru) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006091128A1 (fr) | 2005-02-28 | 2006-08-31 | Viktor Vasilievich Avdeev | Procede de traitement de graphite et reacteur pour sa mise en oeuvre |
CN104495834A (zh) * | 2015-01-16 | 2015-04-08 | 黑龙江科技大学 | 气态氧化剂替代固、液态氧化剂制备可膨胀石墨的方法 |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA2410055A1 (en) * | 2000-05-24 | 2001-11-29 | Superior Graphite Co. | Method of preparing graphite intercalation compounds and resultant products |
DE10140490A1 (de) * | 2000-08-18 | 2002-04-11 | Graftech Inc | Expansionsfähiger Graphit und Herstellungsverfahren |
CN101161338B (zh) * | 2007-11-16 | 2010-06-02 | 南京理工大学 | 负载Cu2O微粒子的氧化石墨及其制备方法 |
CN101161336B (zh) * | 2007-11-16 | 2010-06-02 | 南京理工大学 | 负载纳米金属银粒子的氧化石墨及其制备方法 |
US8691174B2 (en) * | 2009-01-26 | 2014-04-08 | Dow Global Technologies Llc | Nitrate salt-based process for manufacture of graphite oxide |
CN102286753A (zh) * | 2011-05-30 | 2011-12-21 | 黑龙江科技学院 | 一种制备高纯低硫膨胀石墨方法 |
CN102424532B (zh) * | 2011-08-31 | 2013-10-23 | 燕山大学 | 一种玻璃基底上石墨烯透明导电薄膜的制备方法 |
CN102701195B (zh) * | 2012-06-27 | 2014-06-11 | 华南理工大学 | 使用臭氧制备可膨胀石墨的方法 |
CN102745684B (zh) * | 2012-07-24 | 2013-09-11 | 南京理工大学 | 一种硝化细菌生物氧化石墨及其制备方法 |
CN102745683B (zh) * | 2012-07-24 | 2013-09-25 | 南京理工大学 | 一种生物氧化石墨及其制备方法 |
CN105036119B (zh) * | 2015-06-30 | 2017-05-03 | 黑龙江省科学院高技术研究院 | 一种层间插层石墨制取方法 |
KR102233101B1 (ko) * | 2015-12-24 | 2021-03-29 | 한국전자기술연구원 | 산화그라파이트 제조장치 및 산화그라파이트 제조방법 |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1186727A (en) * | 1967-04-28 | 1970-04-02 | Dow Chemical Co | Process for producing Expanded Graphite |
WO1990015022A1 (en) * | 1989-05-29 | 1990-12-13 | Institut Khimii Dalnevostochnogo Otdelenia Akademii Nauk Sssr | Hydrate of carbon hydroxide and method of obtaining it |
US5057297A (en) * | 1987-07-01 | 1991-10-15 | Koa Oil Company, Limited | Method for producing elastic graphite structures |
US5352430A (en) * | 1992-07-17 | 1994-10-04 | Inland Steel Company | Method of manufacturing intercalation compounds |
RU2038337C1 (ru) * | 1991-06-27 | 1995-06-27 | Авдеев Виктор Васильевич | Гибкая графитовая фольга и способ ее получения |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5562807A (en) * | 1978-11-06 | 1980-05-12 | Agency Of Ind Science & Technol | Production of expanded graphite |
SU1497952A1 (ru) * | 1987-06-10 | 1994-01-30 | МГУ им.М.В.Ломоносова | Способ получения расширенного графита |
EP0305984B1 (en) * | 1987-08-31 | 1994-01-05 | Union Carbide Corporation | Intercalation of graphite |
SU1577244A1 (ru) * | 1987-11-11 | 1995-03-20 | Институт физико-органической химии и углехимии АН УССР | Способ получения терморасширяющегося графита |
SU1594865A1 (ru) * | 1988-05-27 | 1994-01-30 | МГУ им.М.В.Ломоносова | Способ получения расширенного графита |
CN1030535C (zh) * | 1991-12-26 | 1995-12-20 | 清华大学 | 可膨胀石墨制造方法及其装置 |
CN1024818C (zh) * | 1992-07-09 | 1994-06-01 | 清华大学 | 一种制备可膨胀石墨的新方法 |
CN107315291B (zh) * | 2017-07-19 | 2020-06-16 | 深圳市华星光电半导体显示技术有限公司 | 一种goa显示面板及goa显示装置 |
-
1996
- 1996-04-26 EP EP96915254A patent/EP0823398B1/en not_active Expired - Lifetime
- 1996-04-26 CN CN96195007A patent/CN1074747C/zh not_active Expired - Fee Related
- 1996-04-26 WO PCT/RU1996/000106 patent/WO1996033949A1/ru active IP Right Grant
- 1996-04-26 DE DE69606529T patent/DE69606529T2/de not_active Expired - Fee Related
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1186727A (en) * | 1967-04-28 | 1970-04-02 | Dow Chemical Co | Process for producing Expanded Graphite |
US5057297A (en) * | 1987-07-01 | 1991-10-15 | Koa Oil Company, Limited | Method for producing elastic graphite structures |
WO1990015022A1 (en) * | 1989-05-29 | 1990-12-13 | Institut Khimii Dalnevostochnogo Otdelenia Akademii Nauk Sssr | Hydrate of carbon hydroxide and method of obtaining it |
RU2038337C1 (ru) * | 1991-06-27 | 1995-06-27 | Авдеев Виктор Васильевич | Гибкая графитовая фольга и способ ее получения |
US5352430A (en) * | 1992-07-17 | 1994-10-04 | Inland Steel Company | Method of manufacturing intercalation compounds |
Non-Patent Citations (1)
Title |
---|
See also references of EP0823398A4 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006091128A1 (fr) | 2005-02-28 | 2006-08-31 | Viktor Vasilievich Avdeev | Procede de traitement de graphite et reacteur pour sa mise en oeuvre |
CN104495834A (zh) * | 2015-01-16 | 2015-04-08 | 黑龙江科技大学 | 气态氧化剂替代固、液态氧化剂制备可膨胀石墨的方法 |
Also Published As
Publication number | Publication date |
---|---|
DE69606529T2 (de) | 2000-08-31 |
CN1189141A (zh) | 1998-07-29 |
DE69606529D1 (de) | 2000-03-09 |
EP0823398A4 (en) | 1998-04-01 |
EP0823398A1 (en) | 1998-02-11 |
EP0823398B1 (en) | 2000-02-02 |
CN1074747C (zh) | 2001-11-14 |
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