KR101451910B1 - Agent for removing hydrogen sulfide and recycling method of the same - Google Patents

Agent for removing hydrogen sulfide and recycling method of the same Download PDF

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KR101451910B1
KR101451910B1 KR1020140037017A KR20140037017A KR101451910B1 KR 101451910 B1 KR101451910 B1 KR 101451910B1 KR 1020140037017 A KR1020140037017 A KR 1020140037017A KR 20140037017 A KR20140037017 A KR 20140037017A KR 101451910 B1 KR101451910 B1 KR 101451910B1
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hydrogen sulfide
removing agent
remover
powder
loess
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KR1020140037017A
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Korean (ko)
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홍은표
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(주)씨앤지테크
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/34Regenerating or reactivating
    • B01J20/345Regenerating or reactivating using a particular desorbing compound or mixture
    • B01J20/3475Regenerating or reactivating using a particular desorbing compound or mixture in the liquid phase
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/0203Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0225Compounds of Fe, Ru, Os, Co, Rh, Ir, Ni, Pd, Pt
    • B01J20/0229Compounds of Fe
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/06Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
    • B01J20/08Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04 comprising aluminium oxide or hydroxide; comprising bauxite
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/10Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/103Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate comprising silica
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material

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  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

The present invention provides a method of recycling a hydrogen sulfide remover, which is characterized by including the steps of: mixing yellow soil powder including iron oxide (Fe_2O_3), aluminum oxide (Al_2O_3) and silicon oxide (SiO_2), limonite including protein, carbohydrate and fat, and water and extruding the resultant mixture to prepare a hydrogen sulfide remover in a pellet shape; mixing the hydrogen sulfide remover with an object from which hydrogen sulfide is to be removed, to absorb hydrogen sulfide; collecting the hydrogen sulfide remover on which hydrogen sulfide be absorbed, to pulverize the hydrogen sulfide remover; neutralizing and recycling the hydrogen sulfide remover pulverized in a powder state; and drying the recycled hydrogen sulfide remover and supplementing yellow soil powder to prepare a hydrogen sulfide remover, wherein the iron oxide (Fe_2O_3) is included in 40 to 65% by weight. Accordingly, hydrogen sulfide that is a main cause of odor among domestic pollution can be effectively absorbed to be removed. A hydrogen sulfide remover includes yellow soil powder as a main ingredient, thereby removing, and also ammonia, oil, and phosphorus can be removed due to porosity, thereby effectively treating livestock excretion. In addition, a hydrogen sulfide remover can be prepared simply at low cost, and hydrogen sulfide remover on which hydrogen sulfide is adsorbed, can be recycled to be used.

Description

황화수소 제거제 및 황화수소 제거제 재생방법{Agent for removing hydrogen sulfide and recycling method of the same}A hydrogen sulfide removing agent and a hydrogen sulfide removing agent regeneration method,

본 발명은 축산공해 중 악취의 주요성분인 황화수소를 제거할 수 있는 황화수소 제거제 및 황화수소 제거제의 재생방법에 관한 것으로서, 보다 상세하게는 황토분말을 이용하여 흡착되는 황화수소의 양을 크게 증가시키고, 황화수소가 흡착된 황화수소 제거제를 중화하여 다시 황화수소 제거제로 재생할 수 있는 황화수소 제거제의 재생방법에 관한 것이다.The present invention relates to a method for regenerating a hydrogen sulfide removing agent and a hydrogen sulfide removing agent capable of removing hydrogen sulfide which is a main component of an offensive odor during livestock pollution, and more particularly, to a method for regenerating hydrogen sulfide To a regeneration method of a hydrogen sulfide removing agent capable of neutralizing an adsorbed hydrogen sulfide removing agent and regenerating it again as a hydrogen sulfide removing agent.

축산산업은 소위 축산공해라고 일컫는 악취, 분진, 축사배수 등의 문제가 심각한 실정이다. 가축의 사육환경 하에서 발생하는 유해가스는 암모니아, 이산화탄소(CO2), 일산화탄소(CO), 이산화황(SO2), 메탄(CH4) 및 황화수소(H2S) 등이 있다. 이산화황과 메탄이 악취에 미치는 영향은 미비하나, 황화수소는 심각한 악취를 가지는 무색의 기체로 일반적으로 황을 함유하는 단백질의 부패에 의해서 잘 생성되므로, 축산산업의 큰 걸림돌이 된다. The livestock industry has serious problems such as odor, dust, and housing drainage, which are called livestock pollution. The harmful gases generated in the breeding environment of livestock include ammonia, carbon dioxide (CO 2 ), carbon monoxide (CO), sulfur dioxide (SO 2 ), methane (CH 4 ) and hydrogen sulfide (H 2 S). The effect of sulfur dioxide and methane on the odor is insufficient, but hydrogen sulfide is a colorless gas with a serious odor and is normally produced by the decay of sulfur-containing proteins, which is a major obstacle to the livestock industry.

축산산업의 발전에 따라 축산시설의 대규모화되고 사람들의 거주지의 확대로 인하여 축산시설의 악취로 인한 문제는 계속 증가하고 있다. 또한 축산시설뿐만 아니라 음식물 및 축산분뇨의 퇴비화 공정에서 발생되는 악취의 주요 원인은 황화수소에 있으므로 황화수소를 효과적으로 흡착하고 제거하는 제거제의 개발이 필요하다. Due to the development of the livestock industry, the scale of the livestock facilities has been enlarged and the problems caused by the odor of the livestock facilities have been continuously increasing due to the expansion of people's residence. In addition, it is necessary to develop a remover that effectively adsorbs and removes hydrogen sulphide because it is a hydrogen sulphide as a main cause of the odor generated in the composting process of the food and livestock manure as well as the livestock facility.

한편 황토는 레스(Loess)라고도 불리며, 사막이나 빙하에 퇴적한 암분이 바람에 의해 운반되어 퇴적된 것을 말한다. 담황색, 회황색 또는 갈색을 띠고 있으며, 성분 조성에 따라 색깔이 달라진다. 황토는 0.004 내지 0.06 ㎜의 입경을 가지는 것이 보통이며, 다공질로 형성된다. 황토의 광물학적 특징은 기원암석의 종류 및 풍화정도에 따라 달라지는 경향을 보이므로, 산출되는 곳에 따라 다른 조성을 가지게 된다.On the other hand, loess is also called Loess, which means that the rocks deposited in the desert or glacier were carried by the wind and deposited. It is light yellow, yellowish brown or brownish, and its color varies depending on its composition. The loess has a particle diameter of 0.004 to 0.06 mm usually, and is formed of a porous material. The mineralogical characteristics of the loess have a tendency to vary depending on the kind of the origin rock and the degree of weathering, and thus have a different composition depending on the calculated location.

우리나라에서는 산화철을 함유한 규조토와 흙으로 이루어진 상태로 많이 산출되며, 특히 전라남도 지방의 황토는 산화철을 많이 함유하고 있어 붉은 색이 강한 경향이 나타난다. 황토의 구성 물질은 광물, 비정질물질 및 유기물을 포함하고 있으며, 광물 속에는 점토광물과 석영 및 기타 광물을 포함하고 있다. In Korea, diatomaceous earth and soil containing iron oxide are produced in large quantities. In particular, yellow loess in Jeollanamdo province tends to have strong red color because it contains a lot of iron oxide. The constituents of the loess include minerals, amorphous materials and organic matter, and clay minerals, quartz and other minerals in the minerals.

황토의 다공성은 다양한 물질을 흡착하는 데에 효과가 있는 것으로 알려졌으며, 한국등록특허 제10-0357765호에서는 부직포, 활성탄, 제올라이트 및 황토 중 1종 또는 2종 이상으로 구성된 탈취필터를 제조방법에 대해 개시한다. The porosity of the loess is known to be effective for adsorbing various substances, and in Korean Patent No. 10-0357765, a deodorizing filter composed of one or more of nonwoven fabric, activated carbon, zeolite, .

그러나 제조된 탈취필터는 황화수소에 대한 탈취효과가 크지 않으며, 탈취필터를 재생하여 사용할 수 없는 단점이 있다. 따라서 악취 제거 성능이 보다 증가되고, 제조 효율이 좋으며, 황화수소 제거제를 재생하여 사용할 수 있는 방법이 필요하다.However, the produced deodorization filter has a disadvantage that the deodorization effect on hydrogen sulfide is not large and the deodorization filter can not be used again. Therefore, there is a need for a method capable of regenerating and using the hydrogen sulfide removing agent because the malodor removing performance is increased, the manufacturing efficiency is good, and the like.

본 발명은, 철이온 함량이 많은 황토를 이용하여 축산공해의 큰 문제인 악취를 제거할 수 있는 황화수소 제거제를 제공하고, 또한 황화수소를 흡착한 황화수소제거제를 간단한 공정을 통하여 재생하고, 이를 다시 사용할 수 있는 방법을 제공하는데 목적이 있다.The present invention provides a hydrogen sulfide removing agent capable of removing odor which is a big problem of livestock pollution by using yellow loess having a large amount of iron ion content and is also capable of regenerating a hydrogen sulfide removing agent adsorbing hydrogen sulfide through a simple process, A method is provided.

본 발명은, 산화철(Fe2O3), 산화알루미늄(Al2O3) 및 산화규소(SiO2)를 포함하는 황토분말, 단백질, 탄수화물 및 지방질을 포함하는 갈철석 및 물을 혼합하고 압출하여 펠릿형상의 황화수소 제거제를 제조하는 단계; 상기 황화수소 제거제를 황화수소 제거 대상물과 혼합하여 황화수소를 흡착하는 단계; 황화수소가 흡착된 황화수소 제거제를 회수하여 분쇄하는 단계; 분쇄되어 분말 상태인 황화수소 제거제를 중화하여 재생하는 단계; 및 재생된 황화수소 제거제를 건조하고, 황토분말을 보충하여 황화수소 제거제를 제조하는 단계를 포함하며, 상기 산화철(Fe2O3)은 40 내지 65중량%로 포함되는 것을 특징으로 하는 황화수소 제거제의 재생방법을 제공한다.The present invention, iron oxide (Fe 2 O 3), aluminum oxide (Al 2 O 3) and silicon oxide ocher powder comprising a (SiO 2), a pellet by mixing galcheolseok and water containing protein, carbohydrate and fat, and extruding Lt; RTI ID = 0.0 > hydrogen sulfide < / RTI > Mixing the hydrogen sulfide removing agent with a hydrogen sulfide removing object to adsorb hydrogen sulfide; Recovering and pulverizing the hydrogen sulfide-removing agent adsorbed by hydrogen sulfide; Neutralizing and recovering powdered hydrogen sulfide scavenger; And a step of drying the regenerated hydrogen sulfide removing agent and replenishing the loess powder to prepare a hydrogen sulfide removing agent, wherein the iron sulfide (Fe 2 O 3 ) is contained in an amount of 40 to 65 wt% .

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또한 상기 황화수소 제거제를 제조하는 단계는, 황토분말을 채취하고 노광에서 3년간 건조하는 단계를 더 포함할 수 있다.The step of preparing the hydrogen sulfide removing agent may further include the step of collecting the loess powder and drying it for 3 years in the exposure.

또한 상기 황화수소 제거제를 중화하여 재생하는 단계는, 알칼리 용액을 첨가하고 공기를 불어넣어 황을 흡착하여 불용성으로 변화된 황화수소 제거제를 수용성을 변화시킬 수 있다. In addition, in the step of neutralizing and regenerating the hydrogen sulfide removing agent, an alkali solution may be added, and air may be blown in to adsorb sulfur to change the water solubility of the hydrogen sulfide removing agent that has been insolubilized.

또한 상기 알칼리 용액은 수산화나트륨(NaOH), 수산화칼륨(KOH), 수산화암모늄(NH4OH) 및 수산화리튬(LiOH)으로 이루어진 군에서 선택된 어느 하나 이상인 것을 특징으로 할 수 있다. Also, the alkali solution can be characterized by at least one selected from the group consisting of sodium hydroxide (NaOH), potassium hydroxide (KOH), ammonium hydroxide (NH 4 OH) and lithium hydroxide (LiOH).

본 발명의 따른 황화수소 제거제에 따르면 축산공해 중 악취의 주요 원인인 황화수소를 매우 효율적으로 흡착하여 제거할 수 있다. 황토분말을 주성분으로 하여 악취 제거가 가능하고, 다공성으로 인하여 암모니아, 유분, 인의 제거도 가능하여, 축산 분뇨의 처리에 매우 효과적이다. 또한 제조가 간단하여 저비용으로 생산할 수 있으며, 황화수소가 흡착된 황화수소 제거제는 다시 중화과정을 통하여 재생이 가능하다.The hydrogen sulfide removing agent according to the present invention can adsorb and remove hydrogen sulfide, which is a main cause of odor during livestock pollution, very efficiently. It is possible to remove odor by using loess powder as a main component, and it is possible to remove ammonia, oil and phosphorus because of porosity, and is very effective in the treatment of animal manure. In addition, it can be produced at low cost with simple production, and the hydrogen sulfide-removing agent capable of adsorbing hydrogen sulfide can be regenerated again through the neutralization process.

도 1은 본 발명의 실시예에 따른 황화수소 제거제의 원료인 황토분말을 채취한 사진이다.
도 2는 본 발명의 실시예에 따른 황화수소 제거제의 원료인 황토분말을 채광 후 건조한 상태의 SEM이미지이다.
도 3은 황화수소 제거 효율을 측정하기 위한 장치의 대략적인 구성도이다.
도 4는 본 발명의 일실시예에 따른 황화수소 제거제의 원료인 황토분말의 황화수소에 대한 파과곡선을 나타낸 그래프이다.
도 5는 본 발명의 일실시예에 따른 황화수소 제거제의 원료물질인 황토분말의 종류를 달리하여 황화수소에 대한 파과곡선을 나타낸 그래프이다.
도 6은 본 발명의 일실시예에 따른 황화수소 제거제의 원료물질인 황토분말을 동일부피의 활성탄과 비교한 황화수소에 대한 파과곡선을 나타낸 그래프이다.
도 7은 본 발명의 일실시예에 따른 황화수소 제거제의 원료물질인 황토분말과 활성탄의 메틸메르캅탄에 대한 파과곡선을 나타낸 그래프이다.
도 8은 본 발명의 일실시예에 따른 황화수소 제거제의 원료물질인 황토분말과 활성탄의 트리메틸아민에 대한 파과곡선을 나타낸 그래프이다.
도 9는 본 발명의 일실시예에 따른 황화수소 제거제를 나타낸 사진이다.
도 10은 본 발명의 다른 실시예에 따른 황화수소 제거제의 재생방법을 타나낸 흐름도이다.
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a photograph showing yellow soil powder as a raw material of a hydrogen sulfide removing agent according to an embodiment of the present invention. FIG.
FIG. 2 is an SEM image of a yellow soil powder as a raw material of a hydrogen sulfide removing agent according to an embodiment of the present invention after being mined.
3 is a schematic diagram of an apparatus for measuring hydrogen sulfide removal efficiency.
FIG. 4 is a graph showing a breakthrough curve of hydrogen sulfide as a raw material of a hydrogen sulfide removing agent according to an embodiment of the present invention. FIG.
FIG. 5 is a graph showing breakthrough curves for hydrogen sulfide with different kinds of loess powder, which is a raw material of the hydrogen sulfide scavenger, according to an embodiment of the present invention.
FIG. 6 is a graph showing breakthrough curves of hydrogen sulfide in comparison with the same volume of activated carbon, which is the raw material of the hydrogen sulfide scavenger according to an embodiment of the present invention. FIG.
7 is a graph showing breakthrough curves of methyl mercaptan of loess powder and activated carbon, which are raw materials of a hydrogen sulfide scavenger, according to an embodiment of the present invention.
8 is a graph showing breakthrough curves of trimethylamine in yellow clay powder and activated carbon, which are raw materials of the hydrogen sulfide scavenger according to an embodiment of the present invention.
9 is a photograph showing a hydrogen sulfide removing agent according to an embodiment of the present invention.
10 is a flowchart illustrating a method of regenerating a hydrogen sulfide remover according to another embodiment of the present invention.

본 발명자는 가축의 사육환경에서 발생하는 유해가스 중 악취의 주요원인인 황화수소(H2S)를 제거하기 위해 노력하던 중 산화철(Fe2O3) 성분이 황화수소와 결합하여 흡착되는 것을 확인하여, 황토분말에 포함되어 있는 산화철 성분을 최적의 조성으로 제조하여 흡착능력을 증가시킨 황화수소 제거제를 완성하였다. 또한 황화수소가 흡착된 제거제를 중화처리 과정을 통하여, 황화수소 제거능력 및 유분 흡착성을 회복시키는 황화수소 제거제 재생방법을 완성하였다. The inventor of the present invention confirmed that iron oxide (Fe 2 O 3 ) component was adsorbed by bonding with hydrogen sulfide while trying to remove hydrogen sulfide (H 2 S) which is a main cause of bad odor in harmful gas generated in a living environment of livestock, The hydrogen sulfide scavenging agent with improved adsorption capacity was prepared by preparing the iron oxide component contained in the loess powder with the optimum composition. In addition, a method of regenerating a hydrogen sulfide removing agent to recover the hydrogen sulfide removing ability and the oil adsorption property through the neutralization treatment of the hydrogen sulfide absorbing remover was completed.

이하 실시예를 통하여 상세하게 설명하기로 한다.Hereinafter, the present invention will be described in detail with reference to examples.

본 발명은 산화철(Fe2O3), 산화알루미늄(Al2O3) 및 산화규소(SiO2)를 포함하는 황토분말, 단백질, 탄수화물 및 지방질을 포함하는 갈철석 및 물을 혼합하고 압출하여 펠릿형상의 황화수소 제거제를 제조하는 단계; 상기 황화수소 제거제를 황화수소 제거 대상물과 혼합하여 황화수소를 흡착하는 단계; 황화수소가 흡착된 황화수소 제거제를 회수하여 분쇄하는 단계; 분쇄되어 분말 상태인 황화수소 제거제를 중화하여 재생하는 단계; 및 재생된 황화수소 제거제를 건조하고, 황토분말을 보충하여 황화수소 제거제를 제조하는 단계를 포함하며, 상기 산화철(Fe2O3)은 40 내지 65중량%로 포함되는 것을 특징으로 하는 황화수소 제거제의 재생방법을 제공한다.The present invention relates to a method of mixing and extruding calcite and water containing ocher powder, proteins, carbohydrates and fats comprising iron oxide (Fe 2 O 3 ), aluminum oxide (Al 2 O 3 ) and silicon oxide (SiO 2 ) Of a hydrogen sulfide removing agent; Mixing the hydrogen sulfide removing agent with a hydrogen sulfide removing object to adsorb hydrogen sulfide; Recovering and pulverizing the hydrogen sulfide-removing agent adsorbed by hydrogen sulfide; Neutralizing and recovering powdered hydrogen sulfide scavenger; And a step of drying the regenerated hydrogen sulfide removing agent and replenishing the loess powder to prepare a hydrogen sulfide removing agent, wherein the iron sulfide (Fe 2 O 3 ) is contained in an amount of 40 to 65 wt% .

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상기 황화수소 제거제를 제조하는 단계는 황토분말을 채취하고 노광에서 3년간 건조하는 단계를 더 포함할 수 있다.The step of preparing the hydrogen sulfide removing agent may further include a step of collecting the yellow loess powder and drying the exposed yellowish soil for 3 years.

상기 건조 단계에서 노광에서 건조하는 경우 공기와 자외선에 의한 풍화, 침식 등에 의해 비표면적이 80 ㎡/g이상으로 증가될 수 있으며, 황화수소 가스 흡착량뿐만 아니라 유분의 흡착력을 증가시킬 수 있다. In the drying step in the drying step, the specific surface area can be increased to 80 m 2 / g or more by weathering, erosion or the like due to air and ultraviolet ray, and the adsorption capacity of not only hydrogen sulfide gas but also oil can be increased.

상기 황화수소가 흡착된 황화수소 제거제를 회수하여 분쇄하는 단계는 황화수소가 흡착된 황화수소 제거제를 30 내지 100 mesh로 분쇄하여 분말로 형태로 황화수소 제거 대상물과 혼합할 수 있다. The step of recovering and pulverizing the hydrogen sulfide-adsorbed hydrogen sulfide removing agent may be performed by pulverizing the hydrogen sulfide-removing agent adsorbed with hydrogen sulfide into 30 to 100 mesh and mixing with the hydrogen sulfide removing object in the form of powder.

펠릿 형태의 황화수소 제거제는 운반 및 보관이 유리하나, 황화수소가 흡착된 이후에 분쇄를 통하여 표면적을 증가시켜, 황화수소와 용이하게 분리될 수 있도록 하는 것이 바람직하다. The pelletized hydrogen sulfide removing agent is advantageous in transportation and storage, but it is preferable to increase the surface area through pulverization after hydrogen sulfide is adsorbed so that it can be easily separated from hydrogen sulfide.

상기 황화수소 제거제를 중화하여 재생하는 단계는 알칼리 용액을 첨가하고, 공기를 불어넣어 황을 흡착하여 불용성으로 변화된 황화수소 제거제를 수용성을 변화시킬 수 있다. In the step of neutralizing and regenerating the hydrogen sulfide removing agent, an alkali solution may be added, and air may be blown to adsorb sulfur to change the water solubility of the hydrogen sulfide removing agent that has been insolubilized.

여기서 상기 알칼리 용액은 수산화나트륨(NaOH), 수산화칼륨(KOH), 수산화암모늄(NH4OH) 및 수산화리튬(LiOH)으로 이루어진 군에서 선택된 어느 하나 이상일 수 있다. Here, the alkali solution may be at least one selected from the group consisting of sodium hydroxide (NaOH), potassium hydroxide (KOH), ammonium hydroxide (NH 4 OH) and lithium hydroxide (LiOH).

상기 황화수소 제거제에 황화수소가 흡착되면 철이온에 황이 흡착된 상태가 된다. 황화철(Fe2S3)은 불용성이므로 침전되어 재생하기가 어려우나, 알칼리 용액으로 처리하는 경우 수용성인 수산화철(Fe(OH)3)로 변하게 되어 재생이 가능하다.
When hydrogen sulfide is adsorbed on the hydrogen sulfide removing agent, sulfur is adsorbed on the iron ion. Since iron (Fe 2 S 3 ) is insoluble, it is difficult to precipitate and regenerate. However, when it is treated with an alkali solution, it becomes water-soluble iron hydroxide (Fe (OH) 3 ) and can be regenerated.

이하, 본 발명의 이해를 돕기 위하여 바람직한 실시예를 제시하나, 하기 실시예는 본 발명을 예시하는 것일 뿐 본 발명의 범위가 하기 실시예에 한정되는 것은 아니다.
Hereinafter, the present invention will be described in more detail with reference to the following examples. However, the scope of the present invention is not limited to the following examples.

<실시예 1> 황화수소 제거 및 황화수소 제거제 재생&Lt; Example 1 > Removal of hydrogen sulfide and regeneration of hydrogen sulfide removing agent

황화수소 제거제에 황화수소, 메틸메르캅탄 및 트리메틸아민 가스와 반응시켰다. 반응 이후에 황화주소 제거제의 탈취 성능을 분석하였다. The hydrogen sulfide removing agent was reacted with hydrogen sulfide, methyl mercaptan, and trimethylamine gas. After the reaction, the deodorizing performance of the sulphated address remover was analyzed.

황화수소 제거제의 재생과정의 효율성을 측정하기 위해 황화수소 제거제를 종래의 활성탄이 충전된 흡착탑에서 활성탄 대신 황화수소 제거제를 충진하여 축산시설에서 배출되는 황화수소를 통과시켰다. In order to measure the efficiency of the regeneration process of the hydrogen sulfide scavenger, the hydrogen sulfide scavenger was filled with the hydrogen sulfide scavenger instead of the activated carbon in the adsorption tower filled with the conventional activated carbon, and the hydrogen sulfide discharged from the livestock facility was passed through.

상기 흡착탑에서 배출되는 황화수소의 농도가 20 ppm이하일 때 상기 흡착탑에서 상기 황화수소 제거제를 분리하여 분쇄하고, 중화처리 하였다. When the concentration of hydrogen sulfide discharged from the adsorption tower is 20 ppm or less, the hydrogen sulfide removing agent is separated from the adsorption tower, pulverized, and neutralized.

중화처리한 황화수소 제거제를 건조하고, 황토분말을 첨가하여 황화수소 제거제를 재생하였다.
The neutralized hydrogen sulfide removing agent was dried, and yellowing powder was added to regenerate the hydrogen sulfide removing agent.

<실험예 1> 황화수소 제거제의 효능 및 재생방법의 분석<Experimental Example 1> Analysis of efficacy and regeneration method of hydrogen sulfide scavenger

1. 황화수소 제거제의 효능1. The efficacy of hydrogen sulphide remover

먼저 원료로 사용된 황토분말의 조성은 X선 형광분석법(Xray flourescence spectrometry; XRF)을 통하여 분석하였다. The composition of loess powder used as raw material was analyzed by Xray fluorescence spectrometry (XRF).

황토는 지질환경 수문환경, 지형 및 기후에 의하여 성분에 차이가 있으므로 황화수소 제거 효율이 높은 황토를 결정하기 위해 산출지가 상이한 4가지 종류의 황토의 조성을 비교하였다.The composition of four different types of loess was investigated in order to determine loess with high efficiency of removal of hydrogen sulfide because loess has different composition depending on geological environment, hydrological environment, topography and climate.

황토 A는 전라도 지방에서 산출된 것이고, 황토 B는 경상도 지방에서 산출되었다. 황토 C는 수분함량에 따른 제거 효율을 비교하기 위해 상기 황토 B를 상온에서 건조한 것이다. 황토 D는 일본 큐슈지방에서 산출된 것이다. Hwangto A was produced in Jeolla province and Hwangto B was produced in Gyeongsang province. Yellow soil C was dried at room temperature to compare the removal efficiency according to the moisture content. Hwangto D is derived from the Kyushu region of Japan.

도 1은 본 발명의 일실시예에 따른 황화수소 제거제의 원료인 황토분말을 채취한 사진이다. BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a photograph showing yellow soil powder as a raw material of a hydrogen sulfide removing agent according to an embodiment of the present invention. FIG.

황토 AHwangto A 황토 BLoess B 황토 CLoess C 황토 DLoess D Al2O3 Al 2 O 3 27.09%27.09% 26.03%26.03% 27.58%27.58% 3.08%3.08% SiO2 SiO 2 58.74%58.74% 60.71%60.71% 59.17%59.17% 12.48%12.48% Fe2O3 Fe 2 O 3 8.17%8.17% 7.42%7.42% 7.20%7.20% 71.69%71.69% 기타 잔유 성분Other residues 6%6% 5.84%5.84% 6.05%6.05% 12.75%12.75%

표 1은 XRF 분석을 통하여 나타낸 황토의 주요 성분을 나타낸 표이다. Table 1 is a table showing the major components of loess through XRF analysis.

시료의 분석결과 황토 A, B, 및 C는 산화알루미늄 27 내지 28 중량%, 산화규소 58 내지 60중량%, 산화철 7 내지 8 중량%를 포함하고 있었다. 반면에 황토 D는 다른 시료에 비해 매우 많은 산화철을 포함하고 있었으며, 본 발명에 따른 황화수소 제거제의 무기물질을 구성하는 황토분말로 선택되었다. As a result of analysis of the samples, the yellow loess A, B, and C contained 27 to 28 wt% of aluminum oxide, 58 to 60 wt% of silicon oxide, and 7 to 8 wt% of iron oxide. On the other hand, the yellow loess D contained much iron oxide as compared with other samples and was selected as the yellow loose powder constituting the inorganic substance of the hydrogen sulfide removing agent according to the present invention.

도 2는 본 발명의 실시예에 따른 황화수소 제거제의 원료인 황토분말을 채광 후 건조한 상태의 SEM이미지이다. FIG. 2 is an SEM image of a yellow soil powder as a raw material of a hydrogen sulfide removing agent according to an embodiment of the present invention after being mined.

도면을 확인하면, 황화수소 제거제를 제조하는 과정에서 황토분말을 채굴하고 3년간 노광에서 건조하는 경우 다공성이 증가되는 것을 확인하였다. It was confirmed that porosity was increased when yellow loess powder was mined in the process of producing hydrogen sulfide removing agent and dried in exposure for 3 years.

황토 A, B, C, 및 D를 가지고 악취성분 제거 효율을 측정하였다. The removal efficiency of odor components was measured with yellow loess A, B, C, and D.

도 3은 황화수소 제거 효율을 측정하기 위한 장치의 대략적인 구성도이다. 3 is a schematic diagram of an apparatus for measuring hydrogen sulfide removal efficiency.

두 개의 가스 봄베 중 하나는 황화수소를 충전하여 준비하였다. 황화수소 외에 메틸메르캅탄(methylmercaptan) 또는 트라이메틸아민(trimethylamine)을 충전한 가스 봄베를 준비하여 황의 흡착정도를 비교하였다. One of the two gas cylinders was filled with hydrogen sulphide. A gas cylinder filled with methylmercaptan or trimethylamine in addition to hydrogen sulfide was prepared to compare the degree of adsorption of sulfur.

여기서 사용된 황화수소, 메틸머캅탄 및 트라이메틸아민은 질소를 밸런스(balance)가스로 하여 150 내지 300 ppm으로 조정된 것을 구입하였다((주)리가스). 가스 크로마토그래프(gas chromatography; GC, HP, 5890 Series Ⅱ)를 사용하여 성분을 분석하였다. 검출기(detector)는 황화수소 및 메틸메르캅탄의 경우 FPD(Flame Photometric Detector)를 사용하였으며, 트리메틸아민의 경우는 FID(Flame ionization detector)를 사용하였다. 유입온도는 180 ℃이고, 배출온도는 200 ℃이였다.The hydrogen sulfide, methyl mercaptan, and trimethylamine used herein were nitrogen gas balance gases adjusted to 150 to 300 ppm (Li Gas Co., Ltd.). The components were analyzed using gas chromatography (GC, HP, 5890 Series II). The detector used FPD (Flame Photometric Detector) for hydrogen sulfide and methyl mercaptan, and Flame ionization detector (FID) for trimethylamine. The inlet temperature was 180 ° C and the discharge temperature was 200 ° C.

상기 시료를 30 내지 100 mesh로 분쇄하고 유자관(U-tube)에 투입하였다. 유자관 하부에 유리필터(glass filter)는 투입된 분말 입자를 지지하는 반면에 황화수소, 메틸메르캅탄 및 트리메틸아민 가스는 50 ㎖/min으로 통과시켰다.The sample was pulverized to 30 to 100 mesh and put into a U-tube. In the lower part of the citrullus, a glass filter supported powder particles, while hydrogen sulfide, methyl mercaptan, and trimethylamine gas were passed at a flow rate of 50 ml / min.

각각의 시료 0.5 g을 가지고 유자관에서 배출되는 황화수소의 농도를 GC/FPD로 측정하였다. The concentration of hydrogen sulfide discharged from the citrullus was measured by GC / FPD with 0.5 g of each sample.

도 4는 본 발명의 실시예에 따른 황화수소 제거제의 원료인 황토분말의 황화수소에 대한 파과곡선을 나타낸 그래프이다. 4 is a graph showing breakthrough curves of hydrogen sulfide as a raw material of a hydrogen sulfide removing agent according to an embodiment of the present invention.

도면을 확인하면, 유자관에서 배출되는 황화수소의 농도는 질소의 흐름에 비해 공기가 흐를 때 더 많을 황화수소가 제거되는 것으로 나타났다. 황토 표면의 금속이온이 공기 중 산소에 의해 황화수소를 제거하기 때문이다. The results show that the concentration of hydrogen sulfide discharged from the citrus canal is higher than that of the nitrogen stream when more hydrogen sulfide is removed. This is because metal ions on the surface of the loess soil remove hydrogen sulfide by oxygen in the air.

도 5는 본 발명의 실시예에 따른 황화수소 제거제의 원료물질인 황토분말의 종류를 달리하여 황화수소에 대한 파과곡선을 나타낸 그래프이다. FIG. 5 is a graph showing breakthrough curves for hydrogen sulfide with different types of loess powder, which is a raw material of the hydrogen sulfide removing agent, according to an embodiment of the present invention.

도면을 확인하면 황토 D를 사용한 경우에 가장 많은 황화수소가 제거되었음을 확인하였다. 또한 황토의 무게의 변화를 측정한 결과 황토 D를 사용한 경우 약 30%도의 무게가 증가하였다. It was confirmed that most of the hydrogen sulfide was removed by using the yellow soil D. As a result of measuring the change of the weight of the loess, the weight of loess D was increased by about 30%.

도 6은 본 발명의 실시예에 따른 황화수소 제거제의 원료물질인 황토분말을 동일부피의 활성탄과 비교한 황화수소에 대한 파과곡선을 나타낸 그래프이다. 6 is a graph showing breakthrough curves of hydrogen sulfide in comparison with the same volume of activated carbon, which is the raw material of the hydrogen sulfide scavenger according to the embodiment of the present invention.

상기 활성탄(Kurary사 제품)은 구입하여 가공하지 아니하고 그대로 사용하였으며, 같은 부피를 사용한 경우 공조용 활성탄이나 황토가 동일한 양의 황화수소 제거율을 나타내었다. The activated carbon (manufactured by Kurary) was used without being processed and used as it was. When the same volume was used, the same amount of hydrogen sulfide removal rate was exhibited by the activated carbon or the loess for air conditioning.

도 7은 본 발명의 실시예에 따른 황화수소 제거제의 원료물질인 황토분말과 활성탄의 메틸메르캅탄에 대한 파과곡선을 나타낸 그래프이다. 7 is a graph showing the breakthrough curves of methyl mercaptan of the loess powder and activated carbon, which are raw materials of the hydrogen sulfide scavenger, according to an embodiment of the present invention.

도면을 확인하면, 동일한 부피를 사용한 경우 황토분말은 메틸메르캅탄에 대해서도 활성탄과 거의 유사한 메틸메르캅탄 제거 효율을 보였다.As shown in the drawing, when the same volume was used, the ocher powder showed methylmercaptan removal efficiency almost similar to that of activated carbon even for methylmercaptan.

도 8은 본 발명의 실시예에 따른 황화수소 제거제의 원료물질인 황토분말과 활성탄의 트리메틸아민에 대한 파과곡선을 나타낸 그래프이다. 8 is a graph showing breakthrough curves of trimethylamine in the yellow coal powder and the activated carbon, which are raw materials of the hydrogen sulfide scavenger according to the embodiment of the present invention.

같은 부피의 원료물질인 황토와 공조용 활성탄은 거의 같은 흡착능력을 나타내는 것으로 확인되었다. It was confirmed that the same volume of raw material, Hwangto, and the air-conditioning activated carbon showed almost the same adsorption capacity.

따라서 상기 황토분말을 원료로 하여 제조된 황화수소 제거제는 황화수소 외에 메틸메르캅탄 및 트리메틸아민에 대한 흡착능력도 보임을 확인하였다. Therefore, it was confirmed that the hydrogen sulfide scavenger prepared from the loess powder was also able to adsorb to methyl mercaptan and trimethylamine in addition to hydrogen sulfide.

2. 황화수소 제거제 재생방법 2. How to regenerate hydrogen sulfide scavenger

도 9는 본 발명의 일실시예에 따른 황화수소 제거제를 나타낸 사진이다. 9 is a photograph showing a hydrogen sulfide removing agent according to an embodiment of the present invention.

도 10은 본 발명의 다른 실시예에 따른 황화수소 제거제의 재생방법을 타나낸 흐름도이다. 10 is a flowchart illustrating a method of regenerating a hydrogen sulfide remover according to another embodiment of the present invention.

먼저 황화수소 제거제를 펠릿 형상으로 제조하여 흡수탑에 충진하였다. First, a hydrogen sulfide removing agent was prepared in the form of pellets and filled in an absorption tower.

폐기물 수집조에서 배출되는 황화수소 가스를 흡수탑에 유입하고 반응시켰다. The hydrogen sulfide gas discharged from the waste collection tank was introduced into the absorption tower and reacted.

[반응식 1][Reaction Scheme 1]

SO4 -2 + 2(CH2O)(유기물) + 2H+ → H2S(gas) ↑ + 2H2O + 2CO2(gas)↑ SO 4 -2 + 2 (CH 2 O) (organic matter) + 2H + → H 2 S (gas) ↑ + 2H 2 O + 2 CO 2 (gas)

Fe(OH)3(aq) + H2S → Fe2S3(solid)↓ + 3H2O Fe (OH) 3 (aq) + H 2 S → Fe 2 S 3 (solid) ↓ + 3H 2 O

2Fe2S3 + 6H2O + 3O2 → 4Fe(OH)3(aq) + 3S2 (solid)↓ 2Fe 2 S 3 + 6H 2 O + 3O 2 → 4Fe (OH) 3 (aq) + 3S 2 (solid) ↓

반응식1을 확인하면 황산이온이 존재한 수용액 속에 유기화합물이 함께 있는 경우 혐기성 분해에 의해 황화수소가 발생되었다. 이 때 황화수소 제거제의 철이온(Fe3+)이 탈취제로서 효과를 발휘하였다. 침전된 황화철은 알카리용액이 첨가되어 호기성이 되면 황과 수산화철로 환원되고, 수산화철은 재생되어 다시 황화수소 제거제를 제조할 수 있었다. Reaction 1 shows that hydrogen sulfide was generated by anaerobic digestion in the presence of organic compounds in aqueous solution containing sulfate ions. At this time, iron ion (Fe 3+ ) of the hydrogen sulfide removing agent exerted an effect as a deodorant. The precipitated iron sulfide was reduced to sulfur and iron hydroxide when the alkali solution was added to the aerobic solution, and the iron hydroxide was regenerated to produce the hydrogen sulfide remover.

도 11은 본 발명의 실시예에 따른 황화수소 제거제의 시간에 따른 황화수소 흡착력을 나타낸 그래프이고, 도 12는 본 발명의 실시예에 따른 황화수소 제거제의 시간에 따른 유기물질의 흡착력을 나타낸 그래프이다. FIG. 11 is a graph showing adsorption of hydrogen sulfide over time of the hydrogen sulfide remover according to an embodiment of the present invention, and FIG. 12 is a graph showing adsorption of organic substances with time of the hydrogen sulfide remover according to an embodiment of the present invention.

도면을 확인하면, 시간이 경화함에 따라 황화수소의 농도가 크게 감소되는 것을 확인하였으며, 또한 황화수소뿐만 아니라 암모니아, 인, 트리메틸아민 및 메틸메르캅탄에 대해서도 뛰어난 흡착력을 나타내어 축산시설의 정화제로 응용하는 경우 다양하게 활용될 수 있음을 확인하였다. As shown in the drawing, it was confirmed that the concentration of hydrogen sulfide was greatly reduced as the time was hardened, and the adsorption power was excellent also for ammonia, phosphorus, trimethylamine and methyl mercaptan as well as hydrogen sulfide, It is confirmed that

이상에서 살펴본 바와 같이 본 발명에 따른 황화수소 제거제에 의하면 저비용으로 용이하게 황화수소를 제거할 수 있다. 특히 다량의 황화수소를 배출하는 축산산업 등에서 높은 효율로 황화수소를 제거하여 악취문제를 해결할 수 있으며, 사용후의 황화수소 제거제는 간단한 공정으로 재생되어 사용할 수 있으므로, 황화수소제거의 효율이 크게 증대된다.
As described above, the hydrogen sulfide removing agent according to the present invention can easily remove hydrogen sulfide at a low cost. In particular, in the livestock industry which discharges a large amount of hydrogen sulfide, it is possible to eliminate the hydrogen sulfide with high efficiency to solve the odor problem, and since the after-use hydrogen sulfide removing agent can be regenerated by a simple process, the efficiency of hydrogen sulfide removal is greatly increased.

본 발명은 한정된 실시예를 참고로 설명되었으나 이는 예시적인 것에 불과하며, 본 기술 분야의 통상의 지식을 가진 자라면 이로부터 다양한 변형 및 균등한 다른 실시예가 가능하다는 점을 이해할 것이다. 따라서, 본 발명의 진정한 기술적 보호 범위는 첨부된 특허청구범위의 기술적 사상에 의하여 정해져야 할 것이다.While the invention has been described with reference to a limited number of embodiments, it is to be understood that the invention is not limited to the disclosed embodiments, but, on the contrary, is intended to cover various modifications and equivalent arrangements included within the spirit and scope of the appended claims. Accordingly, the true scope of the present invention should be determined by the technical idea of the appended claims.

Claims (9)

삭제delete 삭제delete 삭제delete 삭제delete 삭제delete 산화철(Fe2O3), 산화알루미늄(Al2O3) 및 산화규소(SiO2)를 포함하는 황토분말, 단백질, 탄수화물 및 지방질을 포함하는 갈철석 및 물을 혼합하고 압출하여 펠릿형상의 황화수소 제거제를 제조하는 단계;
상기 황화수소 제거제를 황화수소 제거 대상물과 혼합하여 황화수소를 흡착하는 단계;
황화수소가 흡착된 황화수소 제거제를 회수하여 분쇄하는 단계; 분쇄되어 분말 상태인 황화수소 제거제를 중화하여 재생하는 단계; 및 재생된 황화수소 제거제를 건조하고, 황토분말을 보충하여 황화수소 제거제를 제조하는 단계를 포함하며, 상기 산화철(Fe2O3)은 40 내지 65중량%로 포함되는 것을 특징으로 하는 황화수소 제거제의 재생방법.
A mixture of calcite and water containing ocher powder, protein, carbohydrate and fat including iron oxide (Fe 2 O 3 ), aluminum oxide (Al 2 O 3 ) and silicon oxide (SiO 2 ) is mixed and extruded to form a pellet- ;
Mixing the hydrogen sulfide removing agent with a hydrogen sulfide removing object to adsorb hydrogen sulfide;
Recovering and pulverizing the hydrogen sulfide-removing agent adsorbed by hydrogen sulfide; Neutralizing and recovering powdered hydrogen sulfide scavenger; And a step of drying the regenerated hydrogen sulfide removing agent and replenishing the loess powder to prepare a hydrogen sulfide removing agent, wherein the iron sulfide (Fe 2 O 3 ) is contained in an amount of 40 to 65 wt% .
청구항 6에 있어서, 상기 황화수소 제거제를 제조하는 단계는 황토분말을 채취하고 노광에서 3년간 건조하는 단계를 더 포함하는 황화수소 제거제의 재생방법.The method according to claim 6, wherein the step of preparing the hydrogen sulfide removing agent further comprises the step of collecting the loess powder and drying in the exposure for 3 years. 청구항 6에 있어서, 상기 황화수소 제거제를 중화하여 재생하는 단계는 알칼리 용액을 첨가하고 공기를 불어넣어 황을 흡착하여 불용성으로 변화된 황화수소 제거제를 수용성을 변화시키는 것을 특징으로 하는 황화수소 제거제의 재생방법.[Claim 6] The method according to claim 6, wherein the step of neutralizing and regenerating the hydrogen sulfide removing agent comprises adding an alkali solution and blowing air to adsorb sulfur to change the water solubility of the insoluble hydrogen sulfide removing agent. 청구항 8에 있어서, 상기 알칼리 용액은 수산화나트륨(NaOH), 수산화칼륨(KOH), 수산화암모늄(NH4OH) 및 수산화리튬(LiOH)으로 이루어진 군에서 선택된 어느 하나 이상인 것을 특징으로 하는 황화수소 제거제의 재생방법. The method according to claim 8, wherein the alkali solution is reproduction of hydrogen sulfide removal, characterized in that at least one selected from the group consisting of sodium hydroxide (NaOH), potassium hydroxide (KOH), ammonium hydroxide (NH 4 OH) and lithium hydroxide (LiOH) Way.
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