沼氣脫硫器，是一種沼氣運轉裝置，其特性在於(yu) 脫硫瓶內(nei) 的進氣口上銜接一個(ge) 懸空的多孔管，多孔管盡可以長地橫向伸入脫硫瓶內(nei) 腔，多孔管上密布小孔，小孔的孔徑小於(yu) 氧化鐵小顆粒的直徑。利益在於(yu) 多孔管的設置，使與(yu) 氧化鐵小顆粒之間的出氣道麵積大為(wei) 增大，則出氣量大；其次水分部分泡爛氧化鐵顆粒但仍能留存部分出氣孔；再次在於(yu) 多孔管懸空設置，使脫硫瓶內(nei) 水分積壓在懸空多孔管下方，不容易泡爛多孔管周邊的氧化鐵顆粒。
A biogas desulfurizer is a biogas operating device characterized by a suspended porous pipe connected to the inlet of the desulfurization bottle. The porous pipe can extend horizontally into the inner cavity of the desulfurization bottle as long as possible, and the porous pipe is densely covered with small holes, with a pore size smaller than the diameter of small iron oxide particles. The benefit lies in the setting of porous pipes, which greatly increases the area of the air outlet between small iron oxide particles and results in a large air output; Secondly, some of the water soaked iron oxide particles but still retained some of the air vents; Once again, the porous tube is suspended to prevent the accumulation of water in the desulfurization bottle below the suspended porous tube, making it difficult to soak the iron oxide particles around the porous tube.
沼氣脫硫器幹發脫硫是一種簡易而的脫硫辦法，一般情況下適宜用於(yu) 沼氣儲(chu) 氣量小，硫化氫濃度低的沼氣脫硫。幹法脫除沼氣氣體(ti) 中硫化氫（H2S）的配備根底原理是以O2使H2S 氧化成硫或硫氧化物的一種辦法，也可稱為(wei) 幹式氧化法。幹法配備的構成是，在一個(ge) 容器內(nei) 放入填料，填料層有活性炭、氧化鐵等。氣體(ti) 以低流速從(cong) 一端經過容器內(nei) 填料層，硫化氫（H2S）氧化成硫或硫氧化物後，餘(yu) 留在填料層中，汙染後氣體(ti) 沉著器另一端排出。
The dry desulfurization of biogas desulfurizer is a simple and effective desulfurization method, which is generally suitable for biogas desulfurization with small storage capacity and low hydrogen sulfide concentration. The fundamental principle of the dry method for removing hydrogen sulfide (H2S) from biogas gas is a method of using O2 to oxidize H2S into sulfur or sulfur oxides, also known as the dry oxidation method. The composition of the dry method equipment is to place fillers in a container, with a filler layer consisting of activated carbon, iron oxide, etc. The gas passes through the filling layer of the container at a low flow rate from one end, and hydrogen sulfide (H2S) is oxidized to sulfur or sulfur oxides, remaining in the filling layer. After contamination, the gas is discharged from the other end of the sedimenter.
沼氣脫硫器幹式脫硫重要包括主體(ti) 鋼結構、脫硫劑填料、觀察窗、壓力表、溫度表等組件。脫硫塔一般規劃為(wei) 一用一備，替換運用，即一個(ge) 脫硫，一個(ge) 再生。
The dry desulfurization of biogas desulfurizer mainly includes components such as the main steel structure, desulfurizer filler, observation window, pressure gauge, temperature gauge, etc. The desulfurization tower is generally planned as one for use and one for backup, with alternative use, i.e. one for desulfurization and one for regeneration.
幹法脫硫步： Fe2O3 · H2O ＋ 3 H2S = Fe2S3 ＋ 4 H2O （脫硫）
Dry desulfurization step: Fe2O3 · H2O+3 H2S=Fe2S3+4 H2O (desulfurization)
二步： Fe2S3 ＋ 3÷2 O2 ＋ 3 H2O = Fe2O3 · H2O ＋ 2 H2O ＋ 3 S（再生）
Step 2: Fe2S3+3 ÷ 2 O2+3 H2O=Fe2O3 · H2O+2 H2O+3 S (regeneration)
富含硫化氫的沼氣與(yu) 底部入口處荷載高的脫硫劑反映，反映器上部是負載低的脫硫劑層，經過規劃的沼氣空速和線速，幹式脫硫能抵達的精脫硫結果。
The biogas rich in hydrogen sulfide is reflected by the desulfurizer with high load at the bottom inlet, and the upper part of the reflector is a low load desulfurizer layer. After planning the biogas airspeed and line speed, the fine desulfurization results can be achieved through dry desulfurization.
在沼氣進入幹式脫硫塔之前，應設置有冷凝水罐或沼氣顆粒過濾器。該裝置可以鏟除沼氣中攙和的顆粒雜誌，並使得沼氣在進入脫硫前富含必定濕度。
Before biogas enters the dry desulfurization tower, a condensate tank or biogas particle filter should be installed. This device can remove particles mixed in biogas and make biogas rich in certain humidity before entering desulfurization.
當觀察到脫硫劑變色，或係統壓力喪(sang) 失過大時，應替換運用另一個(ge) 脫硫塔。以後的脫硫塔在沼氣放空後，進行天然通風，對脫硫劑進行再生。當再失結果欠安時，應從(cong) 塔體(ti) 底部將廢棄的脫硫劑鏟除，在底部排放廢棄填料的同時，雷同體(ti) 積的新穎脫硫填料參與(yu) 反映器中。
When discoloration of the desulfurization agent or excessive loss of system pressure is observed, another desulfurization tower should be used instead. After the methane is released, the future desulfurization tower will undergo natural ventilation to regenerate the desulfurization agent. When the results are not satisfactory, the waste desulfurizer should be removed from the bottom of the tower body. At the same time as the waste filler is discharged from the bottom, novel desulfurizer fillers of the same volume should be included in the reactor.
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2023-10-31
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