KR20040100184A - activated chemicals of buring for coal - Google Patents

activated chemicals of buring for coal Download PDF

Info

Publication number
KR20040100184A
KR20040100184A KR1020030032421A KR20030032421A KR20040100184A KR 20040100184 A KR20040100184 A KR 20040100184A KR 1020030032421 A KR1020030032421 A KR 1020030032421A KR 20030032421 A KR20030032421 A KR 20030032421A KR 20040100184 A KR20040100184 A KR 20040100184A
Authority
KR
South Korea
Prior art keywords
coal
combustion
boiler
borax
present
Prior art date
Application number
KR1020030032421A
Other languages
Korean (ko)
Other versions
KR100538120B1 (en
Inventor
김종주
서영관
Original Assignee
김종주
서영관
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 김종주, 서영관 filed Critical 김종주
Priority to KR10-2003-0032421A priority Critical patent/KR100538120B1/en
Publication of KR20040100184A publication Critical patent/KR20040100184A/en
Application granted granted Critical
Publication of KR100538120B1 publication Critical patent/KR100538120B1/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B41PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
    • B41JTYPEWRITERS; SELECTIVE PRINTING MECHANISMS, i.e. MECHANISMS PRINTING OTHERWISE THAN FROM A FORME; CORRECTION OF TYPOGRAPHICAL ERRORS
    • B41J2/00Typewriters or selective printing mechanisms characterised by the printing or marking process for which they are designed
    • B41J2/005Typewriters or selective printing mechanisms characterised by the printing or marking process for which they are designed characterised by bringing liquid or particles selectively into contact with a printing material
    • B41J2/01Ink jet
    • B41J2/17Ink jet characterised by ink handling
    • B41J2/175Ink supply systems ; Circuit parts therefor
    • B41J2/17503Ink cartridges
    • B41J2/17506Refilling of the cartridge
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B41PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
    • B41JTYPEWRITERS; SELECTIVE PRINTING MECHANISMS, i.e. MECHANISMS PRINTING OTHERWISE THAN FROM A FORME; CORRECTION OF TYPOGRAPHICAL ERRORS
    • B41J2/00Typewriters or selective printing mechanisms characterised by the printing or marking process for which they are designed
    • B41J2/005Typewriters or selective printing mechanisms characterised by the printing or marking process for which they are designed characterised by bringing liquid or particles selectively into contact with a printing material
    • B41J2/01Ink jet
    • B41J2/17Ink jet characterised by ink handling
    • B41J2/175Ink supply systems ; Circuit parts therefor
    • B41J2/17503Ink cartridges
    • B41J2/17513Inner structure
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B41PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
    • B41JTYPEWRITERS; SELECTIVE PRINTING MECHANISMS, i.e. MECHANISMS PRINTING OTHERWISE THAN FROM A FORME; CORRECTION OF TYPOGRAPHICAL ERRORS
    • B41J2/00Typewriters or selective printing mechanisms characterised by the printing or marking process for which they are designed
    • B41J2/005Typewriters or selective printing mechanisms characterised by the printing or marking process for which they are designed characterised by bringing liquid or particles selectively into contact with a printing material
    • B41J2/01Ink jet
    • B41J2/17Ink jet characterised by ink handling
    • B41J2/175Ink supply systems ; Circuit parts therefor
    • B41J2/17503Ink cartridges
    • B41J2/17536Protection of cartridges or parts thereof, e.g. tape
    • B41J2/1754Protection of cartridges or parts thereof, e.g. tape with means attached to the cartridge, e.g. protective cap
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B41PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
    • B41JTYPEWRITERS; SELECTIVE PRINTING MECHANISMS, i.e. MECHANISMS PRINTING OTHERWISE THAN FROM A FORME; CORRECTION OF TYPOGRAPHICAL ERRORS
    • B41J2/00Typewriters or selective printing mechanisms characterised by the printing or marking process for which they are designed
    • B41J2/005Typewriters or selective printing mechanisms characterised by the printing or marking process for which they are designed characterised by bringing liquid or particles selectively into contact with a printing material
    • B41J2/01Ink jet
    • B41J2/17Ink jet characterised by ink handling
    • B41J2/175Ink supply systems ; Circuit parts therefor
    • B41J2/17503Ink cartridges
    • B41J2/17556Means for regulating the pressure in the cartridge

Abstract

PURPOSE: To provide an agent for promoting combustion of coals capable of removing sulfur generated while combusting the coals and improving a combustion efficiency. CONSTITUTION: The agent comprises borax and oxygenated water in a weight ratio of 1: 10-20. In the agent, a dissolved oxygen in the oxygenated water is 80-100 parts per million.

Description

석탄용 연소촉진제 {activated chemicals of buring for coal}Combustion Accelerator for Coal {activated chemicals of buring for coal}

본 발명은 고체연료인 석탄을 연소하기 직전 석탄 표면에 분사하므로서, 연소시 발생되는 황산화물을 제거할 뿐 아니라, 연소효율이 향상되도록 한 석탄용 연소촉진제에 관한 것이다.The present invention relates to a combustion accelerator for coal, which not only removes sulfur oxides generated during combustion, but also improves combustion efficiency by spraying coal, which is a solid fuel, on the surface of coal just before combustion.

일반적으로 각종 액체 연료나 고체연료 등을 보일러에서 연소시키거나, 폐기물 등을 소각할 때에 발생되는 배기가스에 황산화물과 일산화탄소 등의 유해물질이 함유되어있고, 이러한 유해물질은 대기 오염의 주원인이 되었다.In general, exhaust gases generated when burning various liquid fuels, solid fuels, etc. in a boiler or incineration of wastes contain harmful substances such as sulfur oxides and carbon monoxide, and these harmful substances have become a major cause of air pollution. .

특히, 황산화물을 제거하기 위한 종래의 수단으로서, 각종 연료가 소각될 때 발생되는 배기가스에 수산화칼슘 (Ca(OH)2)를 분사하여, Ca(OH)2+ SO3= CaSO4+ H2O 의 반응식과 같이, 황산화물이 수산화칼슘과 반응되어 석고로 처리하는 방법이 통용되어 왔다.In particular, as a conventional means for removing sulfur oxides, calcium hydroxide (Ca (OH) 2 ) is injected into the exhaust gas generated when various fuels are incinerated, thereby Ca (OH) 2 + SO 3 = CaSO 4 + H 2 As in the reaction scheme of O, a method of treating sulfur oxide with calcium hydroxide and treating with gypsum has been commonly used.

그러나, 이러한 종래의 방법은 황산화물의 완전한 처리가 이루어지지 않을 뿐 아니라, 황산화물을 처리하는 과정 중에 다량의 슬러지가 생성되므로, 이를 처리하기 위한 별개의 집진 장치가 필요하여, 전체 시스템의 설치 및 관리 비용이 많이 소모되는 문제가 있었다.However, such a conventional method is not only complete treatment of sulfur oxides, but also a large amount of sludge is generated during the treatment of sulfur oxides, so a separate dust collector is required to treat the sulfur oxides. There was a problem that the management cost is high.

또한, 고체 연료인 석탄은 세계적으로 매장량이 풍부하여 공급의 안정성과 경제적 측면에서 유리한 조건을 가지고 있음에도 불구하고 유체 연료 및 기체 연료에 비하여, 그 사용이 불편함과 연소 효율의 저하로 인하여 제한적으로 사용되고 있는 실정이다.In addition, coal, which is a solid fuel, has abundant reserves around the world and has favorable conditions in terms of supply stability and economics, and thus it is limited in use due to its inconvenience in use and deterioration in combustion efficiency, compared to fluid fuel and gaseous fuel. There is a situation.

근래에는 석탄의 연소방식을 개선함으로서, 석탄이 갖고 있는 고유한 문제를 해결하기 위한 많은 노력이 있어 왔으며, 특히 석탄 매장량이 풍부한 지역에서는 에너지원으로 석탄 사용을 선호하고 있는 실정이다.In recent years, many efforts have been made to solve the inherent problems of coal by improving the combustion method of coal, and in particular, the region has a preference for using coal as an energy source in abundant coal reserves.

그러나, 석탄의 연소시 배기가스에 함유되어 있는 황은 보일러 및 각종 설비를 부식시켜 수명을 단축시킬 뿐 아니라, 대기 중에 그래로 방출되면 심각한 대기오염을 유발시키는 문제가 제기되었다.However, sulfur contained in the exhaust gas during the combustion of coal not only shortens the lifespan by corroding boilers and various equipments, but also poses a problem of serious air pollution when released into the atmosphere.

때문에, 상기 황을 제거하기 위한 탈황제의 기술이 많이 연구 개발되고 있는 실정이며, 현재까지 알려진 금속산화물 탈황제는 Zn, Fe, Cu, Ca, Mg, V, Mn, Co, Sn, Pb, Cd, Mo, W, Cr 등이며, 이러한 산화물들은 배기가스 정화에 장단점을 갖고 있다.Therefore, a lot of researches and development of the technology of the desulfurization agent for removing the sulfur, metal oxide desulfurization agents known to date Zn, Fe, Cu, Ca, Mg, V, Mn, Co, Sn, Pb, Cd, Mo , W, Cr and the like, and these oxides have advantages and disadvantages for exhaust gas purification.

실험 결과에 의하면, 석탄 배기가스 중에서 H2S 농도를 20ppmv 이하로 줄일 수 있는 1차 활성성분으로 Zn, Fe, Cu, Mn, Ce 등을 들 수 있고, 첨가제로는 Cu, Fe, Mn, Cr, Ce, Co, Mo, Ni 등이 있다.According to the experimental results, Zn, Fe, Cu, Mn, Ce, etc. may be mentioned as primary active ingredients which can reduce the H 2 S concentration in the coal exhaust gas to 20 ppmv or less, and additives include Cu, Fe, Mn, Cr , Ce, Co, Mo, Ni and the like.

현재, 개발된 탈황제 중에서 혼합아연계 탈황제와 망간계 탈황제가 있으며,특히 망간계 탈황제는 망간과 알루미나가 3 : 1의 중량비로 혼합된 화합물이 섭씨 800 도의 H2- H2S 가스 혼합물로부터 황성분을 제거할 수 있다.At present, the honhapah linked desulfurizing agent and a manganese-based desulfurizing agent in the desulfurizing agent development, particularly manganese-based desulfurizing agent is manganese and alumina is 3: weight ratio of the compound is Celsius 800 degrees H 2 mixed at a 1-remove sulfur from H 2 S gas mixture can do.

그러나, 상기 망간계 탈황제는 이를 제조하기 위하여, 분말 상태의 원료를 혼합한 후 건조, 소성 시키고, 경화 공정을 거치는 등의 제조 공정을 거쳐야되기 때문에, 제조 시간이 지연될 뿐 아니라, 이를 제조하기 위한 별개의 설비가 필요하므로, 적은 비용의 에너지원인 석탄에 비하여 탈황제의 원가가 높아 실용화되지 못하고 있는 실정이었다.However, since the manganese desulfurization agent has to go through a manufacturing process such as mixing the raw materials in a powder state, drying, calcining, and curing to prepare them, not only the production time is delayed, Since separate equipment is required, the cost of desulfurization agent is higher than that of coal, which is a low-cost energy source.

또한, 현재까지 개발된 상기 탈황제는 제조를 위한 별개의 설비가 필요하거나, 제조 과정이 복잡한 문제가 있을 뿐 아니라, 그 기능이 탈황에 제한되어 있으며, 석탄의 연소 효율을 증진시키는 기능을 수행할 수 없어 연소 효율을 상상시키기 위하여 별개의 연소 촉진제를 첨가하여야 되는 번거로움이 있었다.In addition, the desulfurization agent developed to date requires a separate facility for the production, there is a complicated problem in the manufacturing process, its function is limited to the desulfurization, and can perform a function to enhance the combustion efficiency of coal. There was no hassle of adding a separate combustion promoter to imagine the combustion efficiency.

본 발명은 상기한 문제를 해결하기 위하여 연구개발된 것으로서, 붕사와 산소수에 의하여 제조된 연소촉진제에 의하여, 석탄의 연소시 발생되는 황을 간단하고 효과적으로 제거할 수 있도록 하는데 그 기술적 과제가 있다.The present invention has been developed in order to solve the above problems, there is a technical problem to be able to remove sulfur generated during the combustion of coal simply and effectively by the combustion accelerator prepared by borax and oxygen water.

본 발명의 다른 기술적 과제는 붕사와 산소수에 함유된 산소에 의하여, 석탄의 연소가 촉진되어 적은 양의 에너지로 연소 효율이 증대되도록 하는데 있다.Another technical problem of the present invention is to promote the combustion of coal by the oxygen contained in borax and oxygen water so that the combustion efficiency is increased with a small amount of energy.

본 발명의 또 다른 기술적 과제는 석탄이 연소되기 직전에 연소 촉진제를 분사시키므로서, 전체 시스템을 경제적으로 운용할 수 있도록 하는데 있다.Another technical problem of the present invention is to inject a combustion accelerator immediately before coal is combusted, so that the entire system can be economically operated.

본 발명의 또 다른 기술적 과제는 붕사에 의하여 전체 시스템의 부식이 방지되므로 고장발생을 없애고 연장되도록 하는데 있다.Another technical problem of the present invention is to prevent corrosion and extend the entire system by borax, thereby eliminating failure and extending.

본 발명은 석탄 연소시 발생되는 황을 제거하고 연소 효율을 증대시키기 위하여, 붕사와 산소소를 1 : 10 ∼20의 중량비로 혼합 조성하고, 산소수의 용존 산소량을 80∼ 100 ppm으로 하는 것이다.In the present invention, in order to remove sulfur generated during coal combustion and increase combustion efficiency, borax and oxygen are mixed at a weight ratio of 1:10 to 20, and the dissolved oxygen amount of oxygen water is 80 to 100 ppm.

석탄이 연소될 때 발생되는 So2는 고온에서 H2O 와 결합하여 H2So4가 붕사 (NaB4O7 10H2O)와 반응되어 H2So4및 Na2So4로 전환되므로서, 황의 제거가 이루어지며, 이러한 반응식은 다음과 같다.Standing so So 2 is generated when the coal is burned is combined with H 2 O in a high temperature, H 2 So 4 is reacted with borax (NaB 4 O7 10H 2 O) converted to H 2 So 4 and Na 2 So 4, sulfur Removal takes place and this scheme is as follows.

상기와 같이 반응이 진행된 후, 산소수와 붕사에 함유되어 있는 산소가 석탄의 연소 효율을 촉진시키며, 특히 상기 산소수는 별개의 산소발생기를 이용하여 용존산소량 80 ∼ 100ppm 으로 제조하는 것이다.After the reaction proceeds as described above, oxygen contained in oxygen water and borax promotes the combustion efficiency of coal, in particular, the oxygen water is prepared in a dissolved oxygen amount of 80 to 100 ppm using a separate oxygen generator.

일반적으로 물은 상온의 대기압하에서 용존산소량이 4 ∼ 7ppm이나, 본 발명은 공지의 산소 발생기를 이용하여 80 ∼ 100ppm의 산소수를 제조하며, 이것을 이용하는 것이다.Generally, although the amount of dissolved oxygen is 4-7 ppm in water under atmospheric pressure of normal temperature, this invention produces 80-100 ppm oxygen water using a well-known oxygen generator, and uses it.

상기 붕사와 산소수의 혼합 비율은 1 : 10 ∼ 20의 중량비가 바람직하며, 붕사의 함유량이 많으면 연소효율이 저하되고 붕사의 함유량이 적으면 탈황 효과가 저하된다.The mixing ratio of the borax and oxygen water is preferably in a weight ratio of 1:10 to 20. When the content of borax is high, the combustion efficiency is lowered. When the content of borax is low, the desulfurization effect is lowered.

또한, 상기 붕사는 고유효능에 의하여 보일러나 배관설비가 부식되는 것을 방지한다.In addition, the borax to prevent corrosion of the boiler or plumbing equipment by the high efficiency.

본 발명의 실시예에 의하여 설명하면 다음과 같다.Referring to the embodiment of the present invention as follows.

〈 실시예 〉<Example>

공지의 산소발생기를 이용하여 용존산소량이 80 ∼ 100ppm의 산소수를 제조한다.Oxygen water of 80-100 ppm of dissolved oxygen amount is manufactured using a well-known oxygen generator.

상기의 산소수를 붕사와 혼합 조성하는 것으로서, 붕사와 산소수의 혼합 중량비를 1 : 10 ∼ 20으로 하여 연소촉진제를 제조한다.Combustion accelerators are prepared by mixing the oxygen water with borax and mixing the weight ratio of borax and oxygen water to 1:10 to 20.

상기에서 제조된 연소촉진제는 석탄이 보일러의 연소실에 투입되기 직전, 스프레이 장치에 의하여 석탄표면에 분사되며, 고온의 보일러 내부에 투입되면 석탄이 연소시 발생되는 So2가 다음과 같이 반응된다.The combustion accelerator prepared above is injected onto the surface of the coal by a spray device immediately before the coal is introduced into the combustion chamber of the boiler. When the coal is injected into the boiler at high temperature, So 2 generated during combustion of the coal is reacted as follows.

즉, So2가 Na2So4로 변환되므로서 소각된 재에 잔존하게 된다.That is, So 2 is converted into Na 2 So 4 and remains in the incinerated ash.

〈 실험 1 〉〈Experiment 1〉

본 발명의 연소 촉진제가 적용된 상태와 적용되지 않은 상태의 보일러 각각의 실험 대상으로 하여 Fly Ash 중의 미연분 상태를 6일동안 체크한 결과가 다음과 같다.The results of checking the unburned state in the fly ash for 6 days using the combustion target of the present invention and the boilers in the unapplied state are as follows.

보일러 (1) : 본 발명의 연소촉진제가 적용된 보일러Boiler (1): Boiler to which the combustion accelerator of the present invention is applied

보일러 (2) : 본 발명의 연소촉진제가 적용되지 않은 보일러Boiler (2): Boiler to which the combustion promoter of the present invention is not applied

A : Fly Ash 중의 미연분 중량 %의 평균치A: average value of unburnt weight% in fly ash

상기에서와 같이, 본 발명의 연소촉진제가 적용된 보일러는 Fly Ash의 미연분이 15.64% 저감되는 효과를 보였다.As described above, the boiler to which the combustion accelerator of the present invention was applied exhibited an effect of 15.64% reduction in the fine powder of fly ash.

〈 실험 2 〉〈Experiment 2〉

본 발명의 연소촉진제가 적용된 상태와 적용되는 않은 각각의 보일러를 자동시켜 증기량과 석탁 사용량을 측정한 결과가 다음과 같다. (단위 ton/hr)As a result of measuring the amount of steam and the amount of turbidity by automating each boiler to which the combustion accelerator of the present invention is applied and not to each other, the results are as follows. (Unit ton / hr)

상기에서와 같이, 연소촉진제가 적용된 보일러(1)의 경우, 석탄사용량에 비해 증기량이 많아 보일러의 효율이 증대됨을 알 수 있다.As described above, in the case of the boiler (1) to which the combustion accelerator is applied, it can be seen that the efficiency of the boiler is increased due to the large amount of steam compared to the coal consumption.

〈 실험 3 〉〈Experiment 3〉

본 발명의 연소촉진제가 적용된 보일러(1)과 적용되지 않은 보일러(2)의 So2의 발생량을 측정한 결과가 다음과 같다.The results of measuring the amount of So 2 generated in the boiler 1 and the boiler 2 to which the combustion accelerator of the present invention was applied are as follows.

t1 ∼ t10 : 10분 간격의 회수t1 to t10: Number of 10 minute intervals

단위 : ppm ( So2의 함유량 )Unit: ppm (content of So 2 )

상기에서와 같이, 본 발명의 연소촉진제가 적용된 보일러(1)의 경우, 보일러(2)에 비하여 약 45%의 So2저감 효과가 나타난다.As described above, in the case of the boiler 1 to which the combustion accelerator of the present invention is applied, an So 2 reduction effect of about 45% occurs as compared to the boiler 2.

상기한 바와 같이, 본 발명은 연소촉진제를 석탄에 적용하므로서, 석탄의 소모량을 절감할 수 있고, 황의 발생을 최소화할 수 있는 것이다.As described above, the present invention is to apply the combustion promoter to the coal, it is possible to reduce the consumption of coal, it is possible to minimize the generation of sulfur.

또한, 석탄에 분사시키는 간단한 방법을 사용하므로, 산업에 적용하기가 쉬우며, 그 제조 또한 간단하므로 저렴한 비용으로 제조하여 쉽게 사용할 수 있는 것이다.In addition, since a simple method of spraying on coal is used, it is easy to apply to the industry, and its manufacture is also simple, so that it can be manufactured and used easily at low cost.

특히, 산소의 공급에 의하여 연소효율이 증대되므로 보일러의 작동에 있어 최대과제인 경제성이 상승되며, 황이 제거되어 사회문제로 대두되고 있는 오염 발생을 억제할 수 있는 것이다.In particular, since the combustion efficiency is increased by supplying oxygen, economic efficiency, which is the biggest problem in the operation of the boiler, is increased, and sulfur can be removed to suppress the occurrence of pollution, which is emerging as a social problem.

또한, 연소촉진제에 함유된 붕사에 의하여 내식성이 보장되므로 보일러 및배관등의 설비가 고장나는 것을 방지하고 전체 수명이 연장되는 것이다.In addition, since the corrosion resistance is ensured by the borax contained in the combustion accelerator to prevent the failure of equipment such as boilers and piping and to extend the overall life.

상기한 본 발명은 보일러 뿐 아니라, 폐기물 소각 등 모든 분야에 쉽게 적응하여 연소 효율의 상승과 황의 제거 효과를 얻을 수 있는 유익한 발명인 것이다.The present invention described above is an advantageous invention that can be easily adapted to all fields such as waste incineration as well as a boiler to obtain an increase in combustion efficiency and removal of sulfur.

Claims (1)

석탄 연소시 발생되는 황을 제거하고 연소효율을 증대시키기 위하여,In order to remove sulfur generated during coal combustion and increase combustion efficiency, 붕사와 산소수를 1 : 10∼20의 중량비로 혼합 조성하고, 상기 산소수의 용존량을 80∼100ppm으로 하여 조성된 것을 특징으로 하는 석탄의 연소촉진제.A combustion promoter for coal, wherein borax and oxygen water are mixed in a weight ratio of 1:10 to 20, and the dissolved amount of oxygen water is 80 to 100 ppm.
KR10-2003-0032421A 2003-05-21 2003-05-21 activated chemicals of buring for coal KR100538120B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR10-2003-0032421A KR100538120B1 (en) 2003-05-21 2003-05-21 activated chemicals of buring for coal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR10-2003-0032421A KR100538120B1 (en) 2003-05-21 2003-05-21 activated chemicals of buring for coal

Publications (2)

Publication Number Publication Date
KR20040100184A true KR20040100184A (en) 2004-12-02
KR100538120B1 KR100538120B1 (en) 2005-12-22

Family

ID=37377604

Family Applications (1)

Application Number Title Priority Date Filing Date
KR10-2003-0032421A KR100538120B1 (en) 2003-05-21 2003-05-21 activated chemicals of buring for coal

Country Status (1)

Country Link
KR (1) KR100538120B1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20180017759A (en) * 2016-08-11 2018-02-21 서태균 Combustion promoting composition for coal and method for prepairing the same
US10988700B2 (en) 2017-09-18 2021-04-27 Lowcarbon Co., Ltd Desulfurization system using catalyst for desulfurization

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20180068353A (en) 2016-12-13 2018-06-22 (주)우성에프엔피 Combuston Accelerator
KR102188541B1 (en) 2019-03-26 2020-12-09 주식회사 올레더 Environment-friendly flammable substance combustion power improver
KR102216893B1 (en) 2019-04-22 2021-02-18 정필진 Method for manufacturing environment-friendly flammable substance combustion power improver

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20180017759A (en) * 2016-08-11 2018-02-21 서태균 Combustion promoting composition for coal and method for prepairing the same
US10988700B2 (en) 2017-09-18 2021-04-27 Lowcarbon Co., Ltd Desulfurization system using catalyst for desulfurization

Also Published As

Publication number Publication date
KR100538120B1 (en) 2005-12-22

Similar Documents

Publication Publication Date Title
CN100387693C (en) Formulation and preparation method of desulfurization agent for assisting combustion of fire coal
CN1193042A (en) High-energy sweetening coal-saving agent
KR100538120B1 (en) activated chemicals of buring for coal
CN101623588A (en) Method for treating waste incineration flue gas by using phosphate
CN102269418B (en) Method for utilizing papermaking sludge to realize desulfuration, denitrification and coal conservation of circulating fluid bed
KR20180068353A (en) Combuston Accelerator
CN107739642A (en) A kind of solid sulphur denitration coke cleaning additive of coal-burning boiler
JPH08192029A (en) Denitrifying and desulfurizing method and device therefor
CN106268283A (en) Cement kiln flue gas removes heavy metal and sulfur nitre pollutant and the method for recycling
CN101077468A (en) Method for decreasing nitrous oxides of fire coal station boiler flue gas
CN106482131A (en) A kind of wastewater treatment field waste gas processing method
KR100960704B1 (en) Composite for removing carbon dioxide from combustion exhaust gas
CN101670223A (en) Method and device for desulfurizing flue gas
KR102216893B1 (en) Method for manufacturing environment-friendly flammable substance combustion power improver
CN104028101B (en) Flue gas desulfurizing and hydrargyrum-removing integral system and technique
CN207722625U (en) A kind of inexpensive mercury pollution control system of coal-burning boiler
KR102188541B1 (en) Environment-friendly flammable substance combustion power improver
FI61041B (en) FOERFARANDE FOER HEL ELLER DELVIS NEUTRALISERING AV DE VID FOERBRAENNING AV SVAVELHALTIGT BRAENSLE BILDADE SURA FOERBRAENNINGSPRODUKTERNA SAMT MEDEL FOER ANVAENDNING VID FOERFARANDET
CN106559989A (en) The process of nitrogen oxides in flue gas stream
CN204962794U (en) Sewage field exhaust treatment device
CN113599761B (en) Petrochemical alkaline residue treatment system and treatment method
CN215428164U (en) Ultralow emission dry desulphurization unit
CN102463031A (en) Fuel coal waste gas desulphurization method
CN107583445A (en) Inexpensive the mercury pollution control system and method for a kind of coal-burning boiler
KR20050118029A (en) Combusting composition of accelerator for scale environmental contaminant reduction/prohibition

Legal Events

Date Code Title Description
A201 Request for examination
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20120105

Year of fee payment: 7

FPAY Annual fee payment

Payment date: 20130225

Year of fee payment: 8

LAPS Lapse due to unpaid annual fee