KR100436203B1 - foam glass and method for manufacture of it - Google Patents
foam glass and method for manufacture of it Download PDFInfo
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- KR100436203B1 KR100436203B1 KR10-2001-0059069A KR20010059069A KR100436203B1 KR 100436203 B1 KR100436203 B1 KR 100436203B1 KR 20010059069 A KR20010059069 A KR 20010059069A KR 100436203 B1 KR100436203 B1 KR 100436203B1
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- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/08—Other methods of shaping glass by foaming
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/50—Glass production, e.g. reusing waste heat during processing or shaping
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/50—Glass production, e.g. reusing waste heat during processing or shaping
- Y02P40/57—Improving the yield, e-g- reduction of reject rates
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Abstract
개시된 본 발명은, 발포성을 증대시킬 수 있게 되고, 또 균질한 발포작용이 이루어지도록 하며, 대형블록의 제조가 가능하게 됨과 아울러 에너지 절감의 효과를 기대할 수 있게 되도록 하기 위한 것이다.The present invention disclosed is to be able to increase the foamability, to make a homogeneous foaming action, to be able to manufacture a large block and to expect the effect of energy saving.
이의 실현을 위하여 본 발명에서는, 폐형광등으로부터 수은 등의 불순물이 제거된 순수 유리분을 150메쉬 이하의 입도로 분쇄하여 모재료로 준비되도록 하는 제1 전처리단계; 1200℃ 이상의 고온에서 소결되지 않는 슬러리상의 분말 이형제를 거푸집의 벽면에 적량 바르는 제2 전처리단계; 상기한 바와 같은 제1 전처리단계를 통하여 준비된 후 720℃ 내외의 온도로 가열된 유리분말 100중량%에 산화되지 않은 흑연질의 탄소 0.5중량%를 가하여 제1 혼합물을 제조하는 가탄단계; 상기한 가탄단계의 실행이 이루어진 후 황산칼륨(K2SO4), 황산나트륨(Na2SO4), 산화철(Fe2O3)의 군에서 선택된 어느 하나 이상의 성분이 미량으로 상기 제1 혼합물에 가하여져 제2 혼합물을 조성하는 산소공급단계; 상기한 제2 전처리단계를 통하여 준비된 거푸집에 상기한 제2 혼합물을 넣고 전기로내에서 분당 3∼5℃의 승온속도로 가열되도록 하는 승온단계; 상기 승온단계를 통해 730∼780℃까지 승온이 이루어졌을 때 이러한 상태를 30분간 유지시키게 되는 1차 가열단계; 상기 1차 가열단계의 실행이 이루어진 제2 혼합물을 930∼980℃의 온도로 30분간 가열하도록 하는 2차 가열단계; 상기 2차 가열단계의 실행이 완료된 상기 제2 혼합물을 공기중에서 자연 공냉시키게 되도록 하는 서냉단계를 포함하여 이루어지는 폐형광등을 이용하는 발포유리의 제조방법이 제공된다.In order to achieve this, the present invention includes a first pretreatment step of pulverizing a pure glass powder from which impurities such as mercury are removed from a waste fluorescent lamp to a particle size of 150 mesh or less to be prepared as a mother material; A second pretreatment step of applying an appropriate amount of slurry-like powder release agent that is not sintered at a high temperature of 1200 ° C. or higher to the wall surface of the formwork; A charcoal step of preparing a first mixture by adding 0.5 wt% of unoxidized graphite carbon to 100 wt% of the glass powder prepared by the first pretreatment step and then heated to a temperature of about 720 ° C .; After the execution of the above-described charcoal step, any one or more components selected from the group of potassium sulfate (K2SO4), sodium sulfate (Na2SO4) and iron oxide (Fe2O3) are added to the first mixture in a trace amount to supply oxygen to form the second mixture. step; A temperature raising step of putting the second mixture into a form prepared through the second pretreatment step and heating at an elevated temperature rate of 3 to 5 ° C. per minute in an electric furnace; A primary heating step of maintaining this state for 30 minutes when the temperature is raised to 730˜780 ° C. through the temperature raising step; A second heating step of heating the second mixture in which the first heating step is performed at a temperature of 930 to 980 ° C. for 30 minutes; Provided is a method for producing a foamed glass using a waste fluorescent lamp comprising a slow cooling step of allowing the second mixture, which has been performed in the second heating step, to be naturally cooled in air.
Description
본 발명은 폐형광등유리를 이용하는 발포유리의 제조방법에 관한 것으로, 보다 상세하게는 산업폐기물 특히 폐형광등 유리를 이용하여 단열성, 미장성, 차음성, 가공성, 강성 등이 우수하도록, 독립기포조직을 갖는 형태로 제조되는 폐형광등유리를 이용하는 발포유리의 제조방법에 관한 것이다.The present invention relates to a method for producing foamed glass using waste fluorescent glass, and more specifically, to use an industrial waste, in particular waste fluorescent glass, so as to have excellent insulation, plastering, sound insulation, processability, rigidity, etc. It relates to a method for producing a foamed glass using a waste fluorescent glass produced in the form having.
일반적으로 발포유리는 독립기포조직의 형태에 따라 단열재 또는 흡음재로 제조되며, 폼유리, 거품유리, 다포(多泡)유리라고도 불리워지고 있다.In general, the foamed glass is made of a heat insulating material or a sound absorbing material depending on the shape of the independent bubble structure, it is also called foam glass, foam glass, polyfoam (多 泡) glass.
대개는 유리가루에 카본지(紙) 등의 발포제(發泡劑)를 혼합하고 내화성(耐火性)이 있는 틀에 넣어서 약 800℃ 정도로 가열하면 유리가 녹으면서 발포 및 팽창현상이 발생되는데, 이러한 상태로 냉각시키게 되면 비로소 발포유리가 제조된다.In general, when glass powder is mixed with a blowing agent such as carbon paper and put into a mold having a fire resistance, and heated to about 800 ° C., the glass melts, causing foaming and expansion. After cooling, the foamed glass is produced.
발포유리는 비중 0.16∼0.4 정도로 가볍고, 내산성 및 내알칼리성이 뛰어나며, 흡수성(吸水性)이 전혀 없는 물리적 성질을 갖고 있기 때문에 단열재로서 건축물의 벽,천정 등에 널리 쓰이고 있다.Foam glass has a specific gravity of 0.16 to 0.4, is light, has excellent acid and alkali resistance, and has no physical absorption. Therefore, it is widely used as a heat insulating material for building walls and ceilings.
한편, 식기의 재료로 이용되는 발포유리는 그 기포가 작고 독립되어 있으며, 하얗게 빛나는 독특한 아름다움을 갖고 있어 식기의 재료로도 널리 사용되고 있다.On the other hand, the foamed glass used as the material of the tableware is small and independent of the bubbles, and has a unique beauty shining white, and is widely used as a material of the tableware.
한편, 그 조성물은 소다석회유리분 혹은 유리연마슬러지와 발포제로서의 수산화인산칼슘 등의 혼합으로 이루어지거나, 소다석회유리분과 탄산칼슘 및 유리물 등의 혼합으로 이루어지기도 한다.On the other hand, the composition consists of a mixture of soda-lime glass powder or glass polishing sludge and calcium phosphate as a blowing agent, or a mixture of soda-lime glass powder, calcium carbonate and glass.
또한, 그 제조방법으로는 대한민국특허청 등록특허공보 등록번호 10-0194107호에 기재된 발명에서와 같이, 1㎜이하의 소다석회 유리분쇄물 혹은 폐유리분쇄물 혹은 유리연마슬러지 100중량부, 수산화인회석 혹은 수산화인산칼슘화합물 2~40 중량부를 혼합한 조성물을 성형한 후 800~1000℃로 열처리하여 소결 및 발포시켜 발포유리를 제조하도록 하고 있다.In addition, the manufacturing method is 100 parts by weight of soda lime glass crushed or waste glass crushed or glass abrasive sludge of 1 mm or less, as in the invention described in the Republic of Korea Patent Publication No. 10-0194107 After molding a composition mixed with 2 to 40 parts by weight of the calcium phosphate compound, heat treatment at 800 to 1000 ℃ to sinter and foam to prepare a foamed glass.
또한, 대한민국특허청 등록특허공보 등록번호 특1994-0000722호에 기재된 발명에서는, 소다석회 유리 파쇄물 100중량부, 탄산칼슘을 0.3-0.4중량부 물유리를 3.0-5.0중량부를 혼합하여 입경이 3mm 이하로 제조된 과립상 베이스 발포층과 소다석회유리 100중량부, 탄산칼슘 0.2-0.3중량부, 무기안료 0.5-2.0중량부, 점토와 알루미나 1.0-2.5중량부 물유리 3.0-4.0중량부를 혼합하여 입경이 3mm 이하로 제조된 과립상 칼라발포층과 입경 1-3mm 크기의 유리질코팅층을 가이드몰드내에 순차적으로 적층하여 프레스 성형한후, 소성하여 용융 발포시켜 다층 발포유리를 제조토록 하고, 또는 전체 발포유리의 두께중 베이스발포층이 65-70%, 칼라발포층 20-25%, 투명유리질코팅층이 10% 두께가 되도록 적층하고, 또는 소성로에서의 용융발포처리는 720℃까지 분당 10℃씩 승온시키고, 720℃에서 15-20분간 유지시킨후, 850℃까지 분당 5℃씩 승온시키고, 850℃에서 30분간 유지시켜 발포 처리한후 분당 3-5℃씩 냉각하도록 하는 다층발포유리의 제조방법을 제공하고 있다.In addition, in the invention described in Korean Patent Application Publication No. 1994-0000722, 100 parts by weight of soda-lime glass crushed matter and 0.3-0.4 parts by weight of calcium carbonate were mixed with 3.0-5.0 parts by weight of water glass to produce a particle diameter of 3 mm or less. The granular base foam layer and 100 parts by weight of soda-lime glass, 0.2-0.3 parts by weight of calcium carbonate, 0.5-2.0 parts by weight of inorganic pigment, 1.0-2.5 parts by weight of clay and alumina 3.0-4.0 parts by weight of water glass The granular color foam layer and the glass coating layer having a particle size of 1-3 mm in size were sequentially laminated in the guide mold, press-molded, fired and melt-foamed to produce a multilayer foam glass, or in the thickness of the entire foam glass. The base foam layer is laminated to 65-70%, the color foam layer 20-25%, and the transparent glass coating layer 10% thick, or the melt-foaming treatment in the kiln is heated up to 720 ° C. by 10 ° C. per minute, 720 ° C. After holding stand 15-20 minutes, the temperature was raised up to 850 per minute by 5 ℃ ℃, kept at 850 ℃ 30 bungan provides a method of manufacturing a multi-layer foam glass to be cooled by 3-5 ℃ per minute after the treatment foam.
또한, 대한민국특허청 등록특허공보 등록번호 10-0262623호에 기재된 발명에서는, 발포유리제조용 유리로서 출발원료에 상관없이 최종 유리성분이 SiO2 60~75중량부, Al2O3 0.5~3중량부, B2O35~15중량부, CaO 3~15중량부, MgO 3~10중량부, Na2O 7~17중량부, As2O3(또는 Sb2O3 또는 Fe2O3 또는 TiO2 또는 망간산화물,또는 구리산화물 또는 니켈산화물 또는 크롬산화물 또는 As2O3와 Sb2O3 Fe2O3 와 TiO2와 망간산화물과 구리산화물과 니켈산화물과 크롬산화물의 혼합물) 0.5~4중량부로 조성되는 발포유리를 제공하고, 또 유리조성물의 210㎛(70메쉬)이하의 분쇄물 100중량부에 탄소 0.05~5중량부를 잘 혼합하여 내열성거푸집에 넣어 터널킬른 혹은 셔틀킬른을 이용하여 800℃~980℃에서 10분~60분간 유지하는 조건으로 소성하여 제조하는 방법을 제공하고 있다.In addition, in the invention described in Korean Patent Application Publication No. 10-0262623, the final glass component is 60 to 75 parts by weight of SiO2, 0.5 to 3 parts by weight of Al2O3, and B2O35 to 15 weights, regardless of the starting material, as the glass for producing foamed glass. Parts, CaO 3-15 parts by weight, MgO 3-10 parts by weight, Na 2 O 7-17 parts by weight, As 2 O 3 (or Sb 2 O 3 or Fe 2 O 3 or TiO 2 or manganese oxide, copper oxide or nickel oxide or chromium oxide or As 2 O 3 and Sb 2 O 3 Fe 2 O 3 and TiO2, manganese oxide, copper oxide, nickel oxide and chromium oxide mixtures) 0.5 to 4 parts by weight of the foamed glass, and a glass composition of 100 to 20 parts by weight of pulverized matter of less than 210㎛ (70 mesh) carbon 0.05 ~ 5 parts by weight is mixed well and put in a heat-resistant die, and using a tunnel kiln or shuttle kiln to provide a method for producing by firing under conditions maintained for 10 minutes to 60 minutes at 800 ℃ ~ 980 ℃.
또한, 대한민국특허청 등록특허공보 등록번호 10-0246755호에 기재된 발명에서는, 폐유리 분말을 200oC ~ 300oC의 온도 및 50Kg/cm2 ~ 70Kg/cm2의 압력조건 하에서 가수분해시키는 단계; 수화된 유리분말에 발포조제를 가하여 이들의 입도가 -325mesh되게 분쇄 조절하는 단계; 상기 입도조절된 수화된 유리원료분말을 용기에 담아 그 겉보기밀도가 0.8 이상 되도록 밀도조절해 주는 단계와; 그리고, 상기 밀도조절된 유리원료분말에 대하여 통상의 소성발포단계, 안정화단계 및 소둔단계를 거치도록 하여 0.3g/㎤ 이하의 밀도 및0.05 Kcal/hmoC 이하의 열전도도를 갖는 발포유리를 얻을 수 있도록 하는 발포유리제조방법을 제공하고 있다.In addition, in the invention described in the Republic of Korea Patent Publication No. 10-0246755, the step of hydrolyzing the waste glass powder at a temperature of 200oC ~ 300oC and pressure conditions of 50Kg / cm2 ~ 70Kg / cm2; Adding a foaming aid to the hydrated glass powder to control the pulverization to have a particle size of -325 mesh; Placing the particle size controlled hydrated glass raw material in a container and adjusting the density so that its apparent density is 0.8 or more; And, through the normal plastic foaming step, stabilization step and annealing step for the density-controlled glass raw material powder to obtain a foamed glass having a density of less than 0.3g / cm3 and thermal conductivity of less than 0.05 Kcal / hmoC It provides a foamed glass manufacturing method.
또한, 대한민국특허청 등록특허공보 등록번호 10-0281793호에 기재된 발명에서는, 미세한 유리분말에 탄소를 균일하게 혼합한 것을 이형제를 도포한 금속형틀에 넣고, 전기머플로에서 1차승온 속도를 5∼8℃/min로 승온시켜 730°∼780℃에 30분간 유지시킨 후 2차 승온 속도를 1°∼5℃로 하여 920°∼980℃에서 30분간 유지시키도록 하는 제조방법 및 유리분말이 150∼200mesh이도록 하는 제조방법이 제공되어 있다.In addition, in the invention described in Korean Patent Application Publication No. 10-0281793, a mixture of carbon and fine glass powder uniformly is put in a metal mold coated with a release agent, and the first temperature increase rate is 5 to 8 in an electric muffle furnace. The method and the glass powder 150-200mesh to maintain the temperature rise at ℃ / min 30 minutes at 730 ° ~ 780 ° C. for 30 minutes and the second temperature increase rate 1 ° ~ 5 ° C. There is provided a manufacturing method.
그러나, 상기한 바와 같은 종래 발포유리의 제조방법들은, 폐유리 특히 폐형광등의 유리분을 재활용할 수 있는 방안이 강구되어 있지 않아 폐형광등 유리에 의한 환경오염의 문제를 방치할 수 밖에 없게 되었고, 또 폐형광등 유리를 재생하지 못함에 따라 자원을 낭비하게 되었으므로, 폐형광등의 유리분을 재활용할 수 있는 방안의 강구가 요구되고 있었다.However, the conventional methods of manufacturing the foamed glass as described above, because there is no way to recycle the waste of glass, especially waste fluorescent glass, there is no choice but to avoid the problem of environmental pollution caused by waste fluorescent glass, In addition, since waste glass cannot be recycled, wastewater is required to devise a way to recycle the glass of waste fluorescent light.
뿐만 아니라, 종래의 발포유리 및 그의 제조방법들은, 그 조성물 중에 많은 가스성분을 함유하지 못하게 되어 발포성을 저하시키게 되고, 따라서 발포유리로서의 특성인 단열성, 미장성, 차음성, 가공성, 강성 등을 극대화시킬 수 없게 된다는 단점이 있었다.In addition, the conventional foamed glass and its manufacturing method, do not contain a lot of gas components in the composition to reduce the foamability, thus maximizing the thermal insulation, plastering, sound insulation, workability, stiffness, etc. that are characteristics as foamed glass There was a disadvantage that you can not.
본 발명은 상기한 바와 같은 종래의 요구에 부응할 수 있게 되도록 하고, 또 종래의 단점을 해소할 수 있게 되도록 하기 위한 것으로, 본 발명의 목적은 발포성을 증대시켜 발포유리로서의 특성인 단열성, 미장성, 차음성, 가공성, 강성 등을 극대화시킬 수 있게 된 폐형광등유리를 이용하는 발포유리의 제조방법을 제공하려는데 있다.The present invention is to be able to meet the conventional needs as described above, and to be able to solve the disadvantages of the conventional, the object of the present invention is to increase the foaming properties, which is characterized as a foam glass, heat insulation, plasticity It is to provide a method for producing foam glass using the waste fluorescent lamp glass that can maximize the sound insulation, processability, rigidity, and the like.
도 1은 본 발명에 의한 방법에 따라 제조되는 발포유리의 열처리 온도 공정을 나타내기 위한 선도,1 is a diagram for showing a heat treatment temperature process of the foamed glass produced according to the method according to the invention,
도 2는 가산작용이 이루어지지 않은 상태에서 제조된 유리블럭의 파단면을 나타내기 위한 현미경 관찰사진,Figure 2 is a microscopic observation photograph showing the fracture surface of the glass block prepared in the state that does not add,
도 3은 가산작용이 이루어지고, 별도의 가탄이 이루어지지 않되, 폐소다석회유리분에 함유되어 있는 K2SO4의 산소공급작용에 따라 제조된 발포유리 블록의 파단면을 나타내기 위한 현미경 관찰사진,Figure 3 is a microscopic observation to show the fracture surface of the foamed glass block is made according to the addition, the addition is not made, and the oxygen supply action of K2SO4 contained in the waste soda lime glass powder,
도 4는 가산작용 및 가탄작용이 이루어진 상태하에서 제조된 발포유리 블록의 파단면을 나타내기 위한 현미경 관찰사진이다.Figure 4 is a microscopic picture for showing the fracture surface of the foamed glass block produced under the addition and the action of the carbonization.
상기한 목적을 달성하기 위하여 본 발명은, 폐형광등으로부터 수은 등의 불순물이 제거된 순수 유리분을 150메쉬 이하의 입도로 분쇄하여 모재료로 준비되도록 하는 제1 전처리단계와, 1200℃ 이상의 고온에서 소결되지 않는 슬러리상의 분말 이형제를 거푸집의 벽면에 적량 바르는 제2 전처리단계와, 상기한 바와 같은 제1 전처리단계를 통하여 준비된 후 720℃ 내외의 온도로 가열된 유리분말 100중량%에 산화되지 않은 흑연질의 탄소 0.5중량%를 가하여 제1 혼합물을 제조하는 가탄단계와, 상기한 가탄단계의 실행이 이루어진 후 황산칼륨(K2SO4), 황산나트륨(Na2SO4), 산화철(Fe2O3)의 군에서 선택된 어느 하나 이상의 성분이 미량으로 상기 제1 혼합물에 가하여져 제2 혼합물을 조성하는 산소공급단계와, 상기한 제2 전처리단계를 통하여 준비된 거푸집에 상기한 제2 혼합물을 넣고 전기로내에서 분당 3∼5℃의 승온속도로 가열되도록 하는 승온단계와, 상기 승온단계를 통해 730∼780℃까지 승온이 이루어졌을 때 이러한 상태를 30분간 유지시키게 되는 1차 가열단계와, 상기 1차 가열단계의 실행이 이루어진 제2 혼합물을 930∼980℃의 온도로 30분간 가열하도록 하는 2차 가열단계와, 상기 2차 가열단계의 실행이 완료된 상기 제2 혼합물을 공기중에서 자연 공냉시키게 되도록 하는 서냉단계를 포함하여 이루어지는 폐형광등을 이용하는 발포유리의 제조방법을 제공한다.In order to achieve the above object, the present invention, the first pre-treatment step to grind the pure glass powder from which impurities such as mercury are removed from the waste fluorescent lamp to a particle size of less than 150 mesh to be prepared as a parent material, and at a high temperature of 1200 ℃ or more Graphite not oxidized to 100% by weight of the glass powder prepared by the second pretreatment step of applying a slurry release agent which is not sintered to the formwork and the first pretreatment step as described above and heated to a temperature of about 720 ° C. One or more components selected from the group of potassium sulfate (K2SO4), sodium sulfate (Na2SO4), and iron oxide (Fe2O3) after the above-described carbonization step is carried out to produce the first mixture by adding 0.5% by weight of carbon of quality A small amount of oxygen is added to the first mixture to form a second mixture, and the die is prepared through the second pretreatment step. The heating step to put the second mixture in the furnace at a heating rate of 3 ~ 5 ℃ per minute, and the first heating to maintain this state for 30 minutes when the temperature is raised to 730 ~ 780 ℃ through the temperature rising step And a second heating step of heating the second mixture on which the first heating step is performed to a temperature of 930 to 980 ° C. for 30 minutes, and the second mixture in which the second heating step is completed, in air. It provides a method for producing a foamed glass using a waste fluorescent lamp comprising a slow cooling step to be naturally air-cooled.
이하에서 상기한 본 발명의 바람직한 실시예를 상세히 설명한다.Hereinafter, a preferred embodiment of the present invention described above will be described in detail.
본 발명은 제1,2 전처리단계와, 가탄단계와, 산소공급단계와, 승온단계와, 1차 가열단계와, 2차 가열단계와, 서냉단계로 이루어지는 발포유리의 제조방법에 관련된다.The present invention relates to a method for producing foamed glass comprising a first and second pretreatment step, a charcoal step, an oxygen supply step, a temperature raising step, a primary heating step, a secondary heating step, and a slow cooling step.
즉, 제1 전처리단계에서 폐형광등으로부터 수은 등의 불순물이 제거된 순수 유리분을 채취하고, 이를 150메쉬 이하의 입도로 분쇄하여 모재료로 준비되도록 한다.That is, in the first pretreatment step, pure glass powder from which impurities such as mercury are removed from the waste fluorescent lamp is collected and ground to a particle size of 150 mesh or less to be prepared as a mother material.
또, 제2 전처리단계에서는 200℃ 이상의 고온에서 소결되지 않는 슬러리상의 분말 이형제를 거푸집의 벽면에 적량 바름으로써, 소결시의 유리분이 거푸집에 붙게 되는 것을 방지할 수 있도록 한다.Further, in the second pretreatment step, by applying an appropriate amount of slurry-like powder release agent that is not sintered at a high temperature of 200 ° C. or higher on the wall surface of the formwork, it is possible to prevent the glass powder during sintering from sticking to the formwork.
또, 상기한 바와 같은 제1 전처리단계를 통하여 준비된 유리분을 제2 전처리단계를 통해 마련된 거푸집에 유리분말 100중량% 기준으로 넣어 720℃ 내외의 온도로 가열시키고 상기 가탄단계에서 산화되지 않은 흑연질의 탄소 0.5중량%를 가하여 제1 혼합물을 제조한다.In addition, the glass powder prepared through the first pretreatment step as described above is added to the mold prepared by the second pretreatment step based on 100% by weight of the glass powder and heated to a temperature of about 720 ° C. 0.5 wt% of carbon is added to prepare a first mixture.
이러한 가탄단계에서는 탄소분이 산화되면서 가스를 생성하게 되며, 특히 탄소분이 720℃ 내외에서 그 분해가 개시되는 것으로 알려져 있다.In this carbonation step, the carbon powder is oxidized to generate gas, and in particular, the decomposition of the carbon powder is known to be started at around 720 ° C.
상기한 가탄단계의 실행이 이루어진 후 산소공급단계에서 황산칼륨(K2SO4), 황산나트륨(Na2SO4), 산화철(Fe2O3)의 군에서 선택된 어느 하나 이상의 성분을 미량 첨가하여 제2 혼합물이 조성되도록 한다.After the above-described carbonization step is performed, a second mixture is formed by adding a small amount of one or more components selected from the group of potassium sulfate (K 2 SO 4), sodium sulfate (Na 2 SO 4), and iron oxide (Fe 2 O 3) in the oxygen supplying step.
또, 상기한 승온단계에서는, 상기 제2 전처리단계를 통하여 준비된 거푸집에 담겨진 제2 혼합물을 전기로내에서 분당 3∼5℃의 승온속도로 가열되도록 하고, 이러한 승온단계를 통해 730∼780℃까지 승온이 이루어졌을 때 상기 1차 가열단계에서 상기한 바와 같은 상태를 30분간 유지시키게 되도록 한다.In the above temperature raising step, the second mixture contained in the formwork prepared through the second pretreatment step is heated in an electric furnace at a temperature increase rate of 3 to 5 ° C. per minute, and the temperature is raised to 730 to 780 ° C. through the temperature rising step. When this is done to maintain the state as described above in the first heating step for 30 minutes.
이에 따라서 730∼780℃까지의 승온이 완료되지 않은 상태에서는 탄소의 분해가 이루어지지지 않는다.As a result, carbon is not decomposed in a state where the temperature increase to 730 to 780 ° C is not completed.
즉, 탄소의 분해 작용은 약 680℃에서부터 시작되므로 승온속도를 분당 3∼5℃ 보다 느리게 하면 유리가 아직 연화되지 않은 상태에서 탄소가 분해되므로 기포를 생성시킬 수 없게 된다.That is, since the decomposition of carbon starts at about 680 ° C., if the temperature increase rate is slower than 3 to 5 ° C. per minute, carbon is decomposed in a state in which the glass is not softened yet, thereby making it impossible to generate bubbles.
따라서, 본 발명에 의한 승온단계를 거치게 되는 유리분 내에는 그 표면이 먼저 유리화되고, 이러한 상태에서 1,2차 가열단계를 차례로 거치게 되므로 충분하고도 균일한 기포의 생성이 이루어지게 된다.Therefore, in the glass powder undergoing the temperature raising step according to the present invention, the surface is first vitrified, and in this state, the first and second heating steps are sequentially performed, thereby generating sufficient and uniform bubbles.
한편, 상기와 같은 1차 가열단계에서의 가열유지 시간은 열추적장치에 의한 분석결과, 730∼780℃에서 30분간 유지될 때 유리 내외부가 10℃이하의 온도차를갖게 된다.On the other hand, the heat holding time in the first heating step as described above has a temperature difference of less than 10 ℃ inside and outside the glass when maintained for 30 minutes at 730 ~ 780 ℃ as a result of analysis by the heat tracking device.
또한, 상기 1차 가열단계의 실행이 이루어진 후 제2 혼합물을 2차 가열단계에서 930∼980℃의 온도로 30분간 가열하도록 하고, 이와 같은 2차 가열단계의 실행이 완료된 상기 제2 혼합물이 서냉단계를 통하여 공기중에서 자연 공냉되도록 한다.In addition, after the first heating step is performed, the second mixture is heated for 30 minutes at a temperature of 930 to 980 ° C. in the second heating step, and the second mixture after the completion of the second heating step is slowly cooled. Allow natural air cooling in the air through the steps.
실시예1Example 1
제1 전처리단계;A first pretreatment step;
폐형광등으로부터 수은 등의 불순물이 제거된 순수 유리분을 조크라샤(Jaw crusher)로 분쇄하여 입도 150메쉬 이하의 것으로 준비하였다.Pure glass powder from which impurities such as mercury were removed from the waste fluorescent lamp was pulverized with a jaw crusher to prepare a particle having a particle size of 150 mesh or less.
제2 전처리단계;A second pretreatment step;
1200℃ 이상의 고온에서 소결되지 않는 슬러리상의 분말 이형제를 300㎜X300㎜X200㎜ 규격의 거푸집 벽면에 적량 바름으로써, 유리물과 거푸집의 원활한 분리가 이루어지도록 하였다.The slurry-like powder releasing agent which was not sintered at a high temperature of 1200 ° C. or higher was appropriately applied to a formwork wall of 300 mm × 300 mm × 200 mm, thereby allowing a smooth separation between the glass and the formwork.
가탄단계;A peat step;
상기 제1 전처리단계를 통해 준비된 유리분말 100중량%를 상기 제2 전처리단계를 통하여 준비된 거푸집에 넣고 720℃ 내외의 온도로 가열하고, 이에 산화되지 않은 흑연질의 탄소 0.5중량%를 V-믹서를 이용해 균일하게 혼합하여 제1 혼합물을 제조하였다.100 wt% of the glass powder prepared through the first pretreatment step was placed in the formwork prepared through the second pretreatment step, and heated to a temperature of about 720 ° C., and 0.5 wt% of the carbon of the non-oxidized graphite was added using a V-mixer. The first mixture was prepared by uniformly mixing.
승온단계;Temperature increase step;
상기한 제2 전처리단계를 통하여 준비된 거푸집에 상기한 제2 혼합물을 넣고전기로내에서 분당 3∼5℃의 승온속도로 가열되도록 하였다(도 1 참조).The above-mentioned second mixture was placed in a die prepared through the second pretreatment step, and was heated in an electric furnace at a temperature increase rate of 3 to 5 ° C. per minute (see FIG. 1).
1차 가열단계;First heating step;
상기 승온단계를 통해 730∼780℃까지 승온이 이루어졌을 때 이러한 상태를 30분간 유지시켰다(도 1 참조).When the temperature was raised to 730 to 780 ° C. through the temperature raising step, this state was maintained for 30 minutes (see FIG. 1).
2차 가열단계;Secondary heating step;
상기 1차 가열단계의 실행이 이루어진 제1 혼합물을 940℃의 온도로 30분간 가열하도록 하였다.The first mixture in which the first heating step was carried out was heated to a temperature of 940 ° C. for 30 minutes.
서냉단계;Slow cooling step;
상기 2차 가열단계의 실행이 완료된 상기 제2 혼합물을 공기중에서 자연 공냉시키게 되도록 하였다(도 1 참조).After completion of the second heating step, the second mixture was allowed to naturally cool in air (see FIG. 1).
즉, 도 1에서와 같은 스케쥴에 따라 가열 소성하여 발포유리를 제조하였으며, 이러한 단계들을 거쳐 제조된 발포유리의 물리적 특성을 미국재료시험규격 (ASTM C552-91)에 따라 시험한 결과는 다음과 같다.That is, foamed glass was manufactured by heating and calcining according to the schedule as shown in FIG. 1, and the physical properties of the foamed glass manufactured through these steps were tested according to the American Material Testing Standard (ASTM C552-91). .
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1) 밀도 : 400 ㎏/㎥1) Density: 400 ㎏ / ㎥
2) 압축강도 : 800 ㎪2) Compressive strength: 800 ㎪
3) 곡강도 : 600 ㎪3) bending strength: 600 ㎪
4) 흡수율 : 2.5%4) Absorption rate: 2.5%
5) 열전도율 : 0.085 W/mㆍK(38℃)5) Thermal Conductivity: 0.085 W / mK (38 ℃)
6) 한편, 발포유리의 파단면을 현미경으로 확대 관찰해 본 결과, 도 2에 나타내어진 것과 같이, 비교적 균일하지 못한 기공이 생성되었으며, 이는 산소성분의 공급 부족으로 추정되었다.6) On the other hand, when the fractured surface of the foam glass was observed under a microscope, as shown in FIG. 2, relatively uneven pores were generated, which was presumed to be a lack of oxygen content.
또한, 큰 블록으로의 발포유리를 제조하는 중에 냉각속도를 느리게 하더라도 블록의 부분적인 파괴가 있었으며, 화석연료를 열원으로 하여 소다석회유리를 용융하게 되었을 때 유리 내에 약 0.3Wt%의 SO3성분이 함유되므로 충분한 상소성분의 공급은 이루어지지 않는다.In addition, the block was partially destroyed even when the cooling rate was slowed down during the manufacture of foamed glass into large blocks. When the soda-lime glass was melted using fossil fuel as a heat source, about 0.3 Wt% of SO 3 was contained in the glass. Therefore, the supply of sufficient component is not made.
실시예2Example 2
제1 전처리단계;A first pretreatment step;
폐형광등으로부터 수은 등의 불순물이 제거된 순수 유리분을 조크라샤(Jaw crusher)로 분쇄하여 입도 150메쉬 이하의 것으로 준비하였다.Pure glass powder from which impurities such as mercury were removed from the waste fluorescent lamp was pulverized with a jaw crusher to prepare a particle having a particle size of 150 mesh or less.
제2 전처리단계;A second pretreatment step;
1200℃ 이상의 고온에서 소결되지 않는 슬러리상의 분말 이형제를 300㎜X300㎜X200㎜ 규격의 거푸집 벽면에 적량 바름으로써, 유리물과 거푸집의 원활한 분리가 이루어지도록 하였다.The slurry-like powder releasing agent which was not sintered at a high temperature of 1200 ° C. or higher was appropriately applied to a formwork wall of 300 mm × 300 mm × 200 mm, thereby allowing a smooth separation between the glass and the formwork.
가탄단계;A peat step;
상기 제1 전처리단계를 통해 준비된 유리분말 100중량%를 상기 제2 전처리단계를 통하여 준비된 거푸집에 넣고 720℃ 내외의 온도로 가열하고, 이에 산화되지 않은 흑연질의 탄소 0.3중량%를 V-믹서를 이용해 균일하게 혼합하여 제1 혼합물을 제조하였다.100 wt% of the glass powder prepared through the first pretreatment step was placed in the formwork prepared through the second pretreatment step and heated to a temperature of about 720 ° C., and 0.3 wt% of the carbon of the non-oxidized graphite was added using a V-mixer. The first mixture was prepared by uniformly mixing.
산소공급단계;Oxygen supply step;
상기한 가탄단계의 실행이 이루어진 후 황산칼륨(K2SO4), 황산나트륨 (Na2SO4), 산화철(Fe2O3)의 군에서 선택된 황산나트륨(Na2SO4) 1중량%를 상기 제1 혼합물에 첨가하여 제2 혼합물을 조성하도록 하였다.After the above-described carbonization step was performed, 1% by weight of sodium sulfate (Na 2 SO 4) selected from the group of potassium sulfate (K 2 SO 4), sodium sulfate (Na 2 SO 4), and iron oxide (Fe 2 O 3) was added to the first mixture to form a second mixture. .
승온단계;Temperature increase step;
상기한 제2 전처리단계를 통하여 준비된 거푸집에 상기한 제2 혼합물을 넣고 전기로내에서 분당 3∼5℃의 승온속도로 가열되도록 하였다(도 1 참조).The above-mentioned second mixture was placed in a form prepared through the second pretreatment step, and heated in an electric furnace at a temperature increase rate of 3 to 5 ° C. per minute (see FIG. 1).
1차 가열단계;First heating step;
상기 승온단계를 통해 730∼780℃까지 승온이 이루어졌을 때 이러한 상태를 30분간 유지시켰다(도 1 참조).When the temperature was raised to 730 to 780 ° C. through the temperature raising step, this state was maintained for 30 minutes (see FIG. 1).
2차 가열단계;Secondary heating step;
상기 1차 가열단계의 실행이 이루어진 제2 혼합물을 860℃의 온도로 30분간 가열하도록 하였다.The second mixture in which the first heating step was carried out was heated to a temperature of 860 ° C. for 30 minutes.
서냉단계;Slow cooling step;
상기 2차 가열단계의 실행이 완료된 상기 제2 혼합물을 공기중에서 자연 공냉시키게 되도록 하였다(도 1 참조).After completion of the second heating step, the second mixture was allowed to naturally cool in air (see FIG. 1).
이러한 다수 단계를 거쳐 제조된 발포유리의 물리적 특성을 미국재료시험규격(ASTM C552-91)에 따라 시험한 결과는 다음과 같다.The physical properties of foamed glass manufactured through these multiple steps were tested in accordance with the American Material Testing Standard (ASTM C552-91).
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1) 밀도 : 210 ㎏/㎥1) Density: 210 ㎏ / ㎥
2) 압축강도 : 730 ㎪2) Compressive strength: 730 ㎪
3) 곡강도 : 570 ㎪3) Bending Strength: 570 ㎪
4) 흡수율 : 0.3%4) Absorption rate: 0.3%
5) 열전도율 : 0.067 W/mㆍK(38℃)5) Thermal Conductivity: 0.067 W / mK (38 ℃)
6) 한편, 발포유리의 파단면을 현미경으로 확대 관찰해 본 결과, 도 3에 나타내어진 것과 같이, 황산나트륨(Na2SO4)을 첨가하지 않은 실시예1에서와 같은 발포유리에 비해 기포가 균일하게 조성되었음을 알 수 있다.6) On the other hand, when the fracture surface of the foam glass was observed under a microscope, as shown in Fig. 3, the bubbles were uniformly formed as compared to the foam glass as in Example 1 without adding sodium sulfate (Na 2 SO 4). Able to know.
실시예3Example 3
제1 전처리단계;A first pretreatment step;
폐형광등으로부터 수은 등의 불순물이 제거된 순수 유리분을 조크라샤(Jaw crusher)로 분쇄하여 입도 150메쉬 이하의 것으로 준비하였고, 또 K2SO4성분이 함유되어 있고, 폐형광등으로부터 얻어진 유리분에 비해 물성이 조금 높은 소다석회 폐유리로부터 얻어진 유리분을 준비하였다.Pure glass powder from which the impurities such as mercury were removed from the waste fluorescent lamp was pulverized with a jaw crusher and prepared with a particle size of 150 mesh or less. Also, K2SO4 component was contained, and the physical properties were compared with those obtained from the waste fluorescent lamp. The glass powder obtained from the slightly high soda-lime waste glass was prepared.
제2 전처리단계;A second pretreatment step;
1200℃ 이상의 고온에서 소결되지 않는 슬러리상의 분말 이형제를 300㎜X300㎜X200㎜ 규격의 거푸집 벽면에 적량 바름으로써, 유리물과 거푸집의 원활한 분리가 이루어지도록 하였다.The slurry-like powder releasing agent which was not sintered at a high temperature of 1200 ° C. or higher was appropriately applied to a formwork wall of 300 mm × 300 mm × 200 mm, thereby allowing a smooth separation between the glass and the formwork.
상기 제1 전처리단계를 통해 준비된 폐형광등으로부터 얻어진 유리분말 50중량%와, 폐소다석회유리로부터 얻어진 유리분 50중량%를 섞어, 상기 제2 전처리단계를 통해 준비된 거푸집에 넣고, 720℃ 내외의 온도로 가열하였다.50 wt% of the glass powder obtained from the waste fluorescent lamp prepared through the first pretreatment step and 50 wt% of the glass powder obtained from the waste soda lime glass are mixed and placed in a form prepared through the second pretreatment step, and the temperature is about 720 ° C. Heated to.
산소공급단계;Oxygen supply step;
상기한 바와 같은 혼합 유리분에, 황산칼륨(K2SO4), 황산나트륨(Na2SO4), 산화철(Fe2O3)의 군에서 선택된 황산나트륨(Na2SO4) 1중량%를 첨가하였다.1 weight% of sodium sulfate (Na2SO4) selected from the group of potassium sulfate (K2SO4), sodium sulfate (Na2SO4), and iron oxide (Fe2O3) was added to the mixed glass powder as mentioned above.
승온단계;Temperature increase step;
상기한 제2 전처리단계를 통하여 준비된 거푸집에 상기한 제2 혼합물을 넣고 전기로내에서 분당 3∼5℃의 승온속도로 가열되도록 하였다(도 1 참조).The above-mentioned second mixture was placed in a form prepared through the second pretreatment step, and heated in an electric furnace at a temperature increase rate of 3 to 5 ° C. per minute (see FIG. 1).
1차 가열단계;First heating step;
상기 승온단계를 통해 730∼780℃까지 승온이 이루어졌을 때 이러한 상태를 30분간 유지시켰다(도 1 참조).When the temperature was raised to 730 to 780 ° C. through the temperature raising step, this state was maintained for 30 minutes (see FIG. 1).
2차 가열단계;Secondary heating step;
상기 1차 가열단계의 실행이 이루어진 제2 혼합물을 880℃의 온도로 30분간 가열하였다.The second mixture in which the first heating step was carried out was heated to a temperature of 880 ° C. for 30 minutes.
서냉단계;Slow cooling step;
상기 2차 가열단계의 실행이 완료된 유리물을 공기중에서 자연 공냉시켜 블록으로 소성되게 하였다(도 1 참조).After completing the second heating step, the glass was naturally cooled in air to be fired into blocks (see FIG. 1).
이러한 다수 단계를 거쳐 제조된 발포유리의 물리적 특성을 미국재료시험규격(ASTM C552-91)에 따라 시험한 결과는 다음과 같다.The physical properties of foamed glass manufactured through these multiple steps were tested in accordance with the American Material Testing Standard (ASTM C552-91).
- 다 음 -- next -
1) 밀도 : 220 ㎏/㎥1) Density: 220 ㎏ / ㎥
2) 압축강도 : 720 ㎪2) Compressive strength: 720 ㎪
3) 곡강도 : 580 ㎪3) Bending Strength: 580 ㎪
4) 흡수율 : 0.3%4) Absorption rate: 0.3%
5) 열전도율 : 0.068 W/mㆍK(38℃)5) Thermal Conductivity: 0.068 W / mK (38 ℃)
6) 한편, 발포유리의 파단면을 현미경으로 확대 관찰해 본 결과, 도 4에 나타내어진 것과 같이, 황산나트륨(Na2SO4)을 첨가하지 않은 실시예1에서와 같은 발포유리에 비해 기포가 균일하게 조성되었음을 알 수 있으며, 실시예2에서와 같은 발포유리보다 치밀한 조직을 갖게 되어 블록의 파괴가 일어나지 않게 됨을 알 수 있다.6) On the other hand, when the fracture surface of the foam glass was observed under a microscope, as shown in Fig. 4, the bubbles were uniformly formed as compared to the foam glass as in Example 1 without adding sodium sulfate (Na 2 SO 4). It can be seen that it has a denser structure than the foamed glass as in Example 2 so that the breakage of the block does not occur.
본 명의 각 실시예에 대한 제조 조건 및 물성을 비교하여 보면 표1에서와 같다.Comparison of the manufacturing conditions and physical properties of each embodiment of the present name is shown in Table 1.
표1Table 1
상기한 바와 같은 본 발명에 의한 발포유리 제조방법은, 발포성을 증대시켜 발포유리로서의 특성인 단열성, 미장성, 차음성, 가공성, 강성 등을 극대화시킬 수있게 될 뿐 아니라, 발포 성분내로의 충분한 산소 공급에 따라 균질한 발포작용이 이루어지고, K2SO4성분으로 인한 블록의 파괴를 방지할 수 있게 되며, 부가적으로는 대형블럭의 제조가 가능하게 됨과 아울러 열처리 온도를 낮추어 에너지 절감의 효과를 기대할 수 있게 된다는데 그 이점이 있다.The foamed glass production method according to the present invention as described above can not only maximize the thermal insulation, plastering, sound insulation, workability, stiffness, etc. that are characteristics of the foamed glass by increasing the foamability, but also sufficient oxygen into the foamed component. As a result of supplying a homogeneous foaming effect, it is possible to prevent the destruction of the block due to K2SO4 components, additionally to manufacture a large block, and to lower the heat treatment temperature to expect energy saving effect It has the advantage.
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KR20030094674A (en) * | 2002-06-07 | 2003-12-18 | 백보기 | Method Preparation of Foam Glass Block for Keeping Warm Insulation Materials of Construction Using Waste Fiber Glass |
KR101110265B1 (en) * | 2009-09-21 | 2012-02-15 | 설용건 | Method for manufacturing multi-cellular body with low expansion and high strenght by using waste liquid crystal display glass and multi-cellular body made by the method |
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US4661137A (en) * | 1984-06-21 | 1987-04-28 | Saint Gobain Vitrage | Process for producing glass microspheres |
JPH01141839A (en) * | 1987-11-27 | 1989-06-02 | Tadahiko Takada | Manufacture of foam glass utilizing shale |
JPH09124327A (en) * | 1995-08-28 | 1997-05-13 | Asahi Glass Co Ltd | Fine hollow glass ball and its production |
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KR100262623B1 (en) * | 1998-03-18 | 2001-01-15 | 이한용 | Glass composition for producing heat insulating foam glass and method for preparing foam glass using the glass composition |
KR100281793B1 (en) * | 1999-01-21 | 2001-02-15 | 배흥진 | Method of light block with waste glass of soda-lime glass silicate |
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US4661137A (en) * | 1984-06-21 | 1987-04-28 | Saint Gobain Vitrage | Process for producing glass microspheres |
JPH01141839A (en) * | 1987-11-27 | 1989-06-02 | Tadahiko Takada | Manufacture of foam glass utilizing shale |
JPH09124327A (en) * | 1995-08-28 | 1997-05-13 | Asahi Glass Co Ltd | Fine hollow glass ball and its production |
KR100262623B1 (en) * | 1998-03-18 | 2001-01-15 | 이한용 | Glass composition for producing heat insulating foam glass and method for preparing foam glass using the glass composition |
KR100281793B1 (en) * | 1999-01-21 | 2001-02-15 | 배흥진 | Method of light block with waste glass of soda-lime glass silicate |
JP2000272942A (en) * | 1999-03-25 | 2000-10-03 | Taiheiyo Cement Corp | Production of artificial lightweight aggregate |
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