JPH0421537B2 - - Google Patents
Info
- Publication number
- JPH0421537B2 JPH0421537B2 JP59194595A JP19459584A JPH0421537B2 JP H0421537 B2 JPH0421537 B2 JP H0421537B2 JP 59194595 A JP59194595 A JP 59194595A JP 19459584 A JP19459584 A JP 19459584A JP H0421537 B2 JPH0421537 B2 JP H0421537B2
- Authority
- JP
- Japan
- Prior art keywords
- desulfurization
- weight
- loess
- parts
- sawdust
- Prior art date
- Legal status (The legal status 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 status listed.)
- Expired - Lifetime
Links
- 239000003795 chemical substances by application Substances 0.000 claims description 28
- 239000007789 gas Substances 0.000 claims description 16
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims description 13
- 229910000037 hydrogen sulfide Inorganic materials 0.000 claims description 13
- 235000007164 Oryza sativa Nutrition 0.000 claims description 8
- 239000010903 husk Substances 0.000 claims description 8
- 235000009566 rice Nutrition 0.000 claims description 8
- 230000003009 desulfurizing effect Effects 0.000 claims description 7
- 239000003513 alkali Substances 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 2
- 240000007594 Oryza sativa Species 0.000 claims 1
- 238000006477 desulfuration reaction Methods 0.000 description 30
- 230000023556 desulfurization Effects 0.000 description 30
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 15
- 241000209094 Oryza Species 0.000 description 7
- 229910052742 iron Inorganic materials 0.000 description 7
- 239000000843 powder Substances 0.000 description 7
- 239000002245 particle Substances 0.000 description 6
- 239000003034 coal gas Substances 0.000 description 3
- 235000014413 iron hydroxide Nutrition 0.000 description 3
- NCNCGGDMXMBVIA-UHFFFAOYSA-L iron(ii) hydroxide Chemical compound [OH-].[OH-].[Fe+2] NCNCGGDMXMBVIA-UHFFFAOYSA-L 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 239000012876 carrier material Substances 0.000 description 2
- 239000004568 cement Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- MBMLMWLHJBBADN-UHFFFAOYSA-N Ferrous sulfide Chemical compound [Fe]=S MBMLMWLHJBBADN-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Industrial Gases (AREA)
Description
<産業上の利用分野>
本発明は石炭ガス等の硫化水素含有ガスからの
硫化水素の除去に有用な脱硫剤に関する。
<従来の技術>
従来、石炭ガス等の硫化水素含有ガスからの硫
化水素を除去するための脱硫剤としては水酸化鉄
を主成分とし、ガスの通過を良くし接触面を大き
くするためにおが屑等を混合したものが使用され
ている。鉄成分としては入手の容易さ、微粉状で
なくガスの通過性がよいことからダライ粉(鋳鉄
削り屑)が主に用いられているが、他にアルミニ
ウム工業の副産物であるLux Masseまたは鉄分
の含有量が多い沼鉄鉱、黄土類も使用されてい
る。
<発明が解決しようとする問題点>
上記のダライ粉を使用した従来法では鉄成分を
水酸化鉄に変えるために長時間の養生期間を要
し、使用後の脱硫剤についてもセメント固化等の
煩雑な後処理を必要とする。また黄土を使用する
場合には粒度が非常に小さいため、おが屑と併用
してもガスの圧損が大きく、低濃度でしか使用で
きなかつた。
<問題点を解決するための手段および作用>
本発明者らは従来、脱硫剤の鉄成分として用い
られている物質の中で、脱硫剤に適した水酸化鉄
の形で鉄分を含有する黄土に着目し、その利用を
検討した。
従来法の場合、ガスと通過をよくし、脱硫剤成
分との接触をよくするための担材として、おがく
ずを使用していた。しかしながらダライ粉と異な
り、黄土は粒子が小さいためガスの圧損が大き
く、使用割合を少なくせざるを得ず、おがくずの
粒度を大きくするなどの方法では解決できなかつ
た。本発明者らは黄土の含有率の高い脱硫剤につ
いて種々検討の結果、もみがらが黄土と併用する
場合の担材として特にすぐれた性能を有すること
を見出し本発明を完成した。
すなわち、本発明の脱硫在は、黄土を主成分と
し、黄土100重量部に対しおがくず35〜65重量部、
もみがら25〜25重量部および必要によりアルカリ
成分3〜15重量部を配合し、混和したことを特徴
とする硫化水素含有ガス用脱硫剤である。
脱硫原理としては硫化水素を含水硫化鉄の形で
捕集するものであるが、この複合体はアルカリの
存在下で安定なので炭酸ナトリウム等のアルカリ
成分の添加が好ましい。
黄土、おがくず、もみがら等の配合比は処理対
象ガス中の硫化水素量、ガスの圧力、脱硫剤の詰
替え周期等により前記範囲内で適宜定めればよ
い。黄土が多くなりすぎると圧損が増加し、少な
すぎると脱硫性能が低下するので好ましくない。
おがくずは1mm以下が80%、1〜3mmが20%と
なるように粒度調整したものが好ましい。もみが
らは通常入手できる形状のままで使用すればよ
い。本発明の脱硫剤は水を添加し、水分20〜65%
に調整して使用する。
使用後の脱硫剤は加熱焼却により硫黄分を回収
したのち通常の産廃物として処理できるが、ダラ
イ粉使用の場合のように鉄分の塊が残らず、セメ
ント原料等への転用も可能である。
<発明の効果>
本発明の脱硫剤は製造、後処理が容易で脱硫性
能がよく、石炭ガス等の硫化水素含有ガスからの
硫化水素の除去、特に比較的低濃度の硫化水素を
含むガスの固定床による脱硫に有効である。
<参考例>
塊状物を除いた黄土と1mm以下が80%、1〜3
mmが20%となるように粒度調整したおがくずを重
量比1:1で混合、よく混和して脱硫剤Aとし
た。一方1mm以下が80%、1〜3mmが20%となる
ように粒度調整したダライ粉とおがくずを重量比
1:1の割合で混和し、水分約40%になるように
水を添加し、以後適宜水を補給しながら40日間養
生したものを脱硫剤Bとした。
この脱硫剤A・Bをそれぞれ第1表に示した水
分に調整し固定床脱硫装置に充填し、硫化水素
4.0±0.5g/Nm3を含むコークス炉ガス(COG)
を流量0.52m3/Hr、流速1.1m/minで通過させ
ガス出口で硫化水素が検出されるまでの時間を比
較した。
<Industrial Application Field> The present invention relates to a desulfurization agent useful for removing hydrogen sulfide from hydrogen sulfide-containing gas such as coal gas. <Conventional technology> Conventionally, desulfurization agents for removing hydrogen sulfide from hydrogen sulfide-containing gases such as coal gas have mainly contained iron hydroxide, and sawdust has been used to improve gas passage and increase the contact surface. A mixture of these is used. As the iron component, dagger powder (cast iron shavings) is mainly used because it is easy to obtain, is not in a fine powder form, and has good gas permeability, but other materials include Lux Masse, a by-product of the aluminum industry, or iron powder. Swamp iron ore and loess, which have a high content, are also used. <Problems to be solved by the invention> The conventional method using the above-mentioned dry powder requires a long curing period to convert the iron component into iron hydroxide, and the desulfurization agent after use also has problems such as cement solidification. Requires complicated post-processing. Furthermore, when using loess, the particle size is very small, so even if it is used in combination with sawdust, the gas pressure loss is large, and it can only be used at low concentrations. <Means and effects for solving the problem> The present inventors have found that among the substances conventionally used as the iron component of desulfurization agents, loess containing iron in the form of iron hydroxide suitable for desulfurization agents. We focused on this and considered its use. In conventional methods, sawdust was used as a carrier material to improve gas passage and contact with the desulfurizing agent component. However, unlike Dalai powder, loess has small particles, so the gas pressure drop is large, so the proportion of use has to be reduced, and this cannot be solved by methods such as increasing the particle size of sawdust. As a result of various studies on desulfurization agents with a high content of loess, the present inventors discovered that rice husk has particularly excellent performance as a carrier material when used in combination with loess, and completed the present invention. That is, the desulfurization solution of the present invention has loess as a main component, and contains 35 to 65 parts by weight of sawdust per 100 parts by weight of loess.
This desulfurizing agent for hydrogen sulfide-containing gas is characterized in that it contains 25 to 25 parts by weight of rice husks and, if necessary, 3 to 15 parts by weight of an alkali component. The principle of desulfurization is to collect hydrogen sulfide in the form of hydrous iron sulfide, but since this composite is stable in the presence of an alkali, it is preferable to add an alkaline component such as sodium carbonate. The blending ratio of loess, sawdust, rice husk, etc. may be appropriately determined within the above range depending on the amount of hydrogen sulfide in the gas to be treated, the pressure of the gas, the period of refilling the desulfurizing agent, etc. Too much loess will increase pressure loss, while too little will reduce desulfurization performance, which is not preferable. It is preferable to adjust the particle size of the sawdust so that 80% is 1 mm or less and 20% is 1 to 3 mm. Rice husks can be used in the form in which they are normally available. The desulfurization agent of the present invention has a moisture content of 20 to 65% by adding water.
Adjust and use. After use, the desulfurization agent can be heated and incinerated to recover the sulfur content and then disposed of as normal industrial waste, but unlike when using dust powder, no lumps of iron remain, and it can also be used as a raw material for cement. <Effects of the Invention> The desulfurization agent of the present invention is easy to manufacture and post-process, has good desulfurization performance, and is useful for removing hydrogen sulfide from hydrogen sulfide-containing gases such as coal gas, especially for gases containing relatively low concentrations of hydrogen sulfide. Effective for fixed bed desulfurization. <Reference example> Loess excluding lumps and 80% less than 1 mm, 1 to 3
Sawdust whose particle size was adjusted so that mm was 20% was mixed at a weight ratio of 1:1 and mixed well to obtain desulfurizing agent A. On the other hand, the particle size was adjusted so that 80% was 1 mm or less and 20% was 1 to 3 mm. Mix the powder and sawdust in a weight ratio of 1:1, add water to make the moisture content about 40%, and then Desulfurization agent B was obtained after curing for 40 days while appropriately supplementing water. These desulfurization agents A and B were adjusted to the moisture content shown in Table 1, and charged into a fixed bed desulfurization equipment, and hydrogen sulfide was removed.
Coke oven gas (COG) containing 4.0±0.5g/ Nm3
was passed through the gas at a flow rate of 0.52 m 3 /Hr and a flow rate of 1.1 m/min, and the time until hydrogen sulfide was detected at the gas outlet was compared.
【表】【table】
【表】
第2表に示した結果から黄土を使用した脱硫剤
Aの方がダライ粉を使用した脱硫剤Bに比較し、
脱硫剤重量当りおよび含有鉄分量当りのH2S吸着
能力が高く、脱硫剤としてすぐれた性能示してい
る。
<実施例、比較例>
黄土50重量部、おがくず25重量部、もみがら20
重量部、Na2CO35重量部を配合してよく混和し、
水分を40%に調整した脱硫剤(脱硫剤C)および
もみがらの代りに同量のおがくずを添加し、同様
に調整した脱硫剤(脱硫剤D)を固定床脱硫装置
に充填し、H2S入口濃度0.15±0.05g/Nm3、
COG流速0.3m/minの条件でCOGを通過させ、
出口におけるH2S濃度と圧損を測定した結果を第
1図および第2図に示す。
おがくずだけを使用した脱硫剤Dでは圧損が大
きく、脱硫性能も低いのに対し、もみがらを併用
した本発明の脱硫剤Cは圧損も低く、きわめてす
ぐれた脱硫性能を有することがわかる。[Table] From the results shown in Table 2, desulfurization agent A using loess is better than desulfurization agent B using lime powder.
It has a high H 2 S adsorption capacity per weight of desulfurization agent and iron content, demonstrating excellent performance as a desulfurization agent. <Examples, Comparative Examples> 50 parts by weight of loess, 25 parts by weight of sawdust, 20 parts by weight of rice husk
parts by weight and 5 parts by weight of Na 2 CO 3 and mix well.
A desulfurization agent (desulfurization agent C) whose moisture content was adjusted to 40% and the same amount of sawdust added instead of rice husks and a desulfurization agent (desulfurization agent D) adjusted in the same manner were charged into a fixed bed desulfurization equipment, and H 2 S inlet concentration 0.15±0.05g/ Nm3 ,
Pass through COG at a COG flow rate of 0.3 m/min,
The results of measuring the H 2 S concentration and pressure drop at the outlet are shown in Figures 1 and 2. Desulfurization agent D using only sawdust has a large pressure loss and low desulfurization performance, whereas desulfurization agent C of the present invention, which uses rice husk in combination, has low pressure loss and extremely excellent desulfurization performance.
第1図、第2図はそれぞれ本発明の脱硫剤Cと
比較用脱硫剤Dの性能を比較した実験例を示すグ
ラフであり、第1図は脱硫装置出口におけるH2S
濃度を、第2図は圧損の状況を示す。
Figures 1 and 2 are graphs showing experimental examples comparing the performance of the desulfurizing agent C of the present invention and the comparative desulfurizing agent D, respectively.
Figure 2 shows the pressure drop situation.
Claims (1)
がくず35〜65重量部、もみがら25〜55重量部およ
び必要によりアルカリ成分3〜15重量部を配合
し、混和したことを特徴とする硫化水素含有ガス
用脱硫剤。1. Hydrogen sulfide, which contains loess as a main component and is made by mixing 100 parts by weight of loess with 35 to 65 parts by weight of sawdust, 25 to 55 parts by weight of rice husk, and 3 to 15 parts by weight of an alkali component if necessary. Desulfurizing agent for containing gas.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59194595A JPS6174642A (en) | 1984-09-19 | 1984-09-19 | Desulfurizing agent for gas containing hydrogen sulfide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59194595A JPS6174642A (en) | 1984-09-19 | 1984-09-19 | Desulfurizing agent for gas containing hydrogen sulfide |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6174642A JPS6174642A (en) | 1986-04-16 |
JPH0421537B2 true JPH0421537B2 (en) | 1992-04-10 |
Family
ID=16327152
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59194595A Granted JPS6174642A (en) | 1984-09-19 | 1984-09-19 | Desulfurizing agent for gas containing hydrogen sulfide |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6174642A (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5059577A (en) * | 1986-09-12 | 1991-10-22 | Hatton John H | Fluid absorbent composition |
US5021390A (en) * | 1986-09-12 | 1991-06-04 | Hatton John H | Liquid hydrocarbon absorbent composition and method |
JP2742070B2 (en) * | 1988-11-10 | 1998-04-22 | 藤沢薬品工業株式会社 | Deodorant |
-
1984
- 1984-09-19 JP JP59194595A patent/JPS6174642A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS6174642A (en) | 1986-04-16 |
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