I. Bayan
Në run juëc cï lɔ̈ɔ̈m yiic, akutnhom de kɔc ye luui në luɔɔi de wɛ̈ɛ̈r de wɛ̈ɛ̈r de wɛ̈ɛ̈r de wɛ̈ɛ̈r de wɛ̈ɛ̈r de wɛ̈ɛ̈r de wɛ̈ɛ̈r de wɛ̈ɛ̈r de wɛ̈ɛ̈r de wɛ̈ɛ̈r de wɛ̈ɛ̈r de wɛ Në kë de gas de fume de nitrification de dust de sulfur de desulfurization, akutnhom de SCR de selective catalytic reduction de nitrification technology, dual alkali de sulfur de desulfurization technology, ammonia de sulfur de desulfurization technology, magnesium de sulfur de desulfurization technology ku jɔl ya teknolojii de dust de desulfurization, ku jɔl ya luɔɔi de luɔɔi kɔrɔ.
II. Boiler denitration dust removal sulfur process
Solution design process: fume gas → compressed fan → residual heat recovery device (coal saver) → heat exchanger → SCR catalytic denitration system → first stage dust removal → second stage dust removal → wet method desulfurization system → heat exchanger → high air emission. Ku ka kony bɛ̈ɛ̈i bɛ̈ɛ̈i bɛ̈ɛ̈i bɛ̈ɛ̈i bɛ̈ɛ̈i bɛ̈ɛ̈i bɛ̈ɛ̈i bɛ̈ɛ̈i bɛ̈ɛ̈i bɛ̈ɛ̈i bɛ
3. Selective Catalytic Reduction SCR Method Process Features
Fɛɛrɛ ye cɔla Selective Catalytic Reduction (SCR) ye cɔla denitration ye cɔla denitration ye cɔla denitration ye cɔla denitration ye cɔla denitration ye cɔla denitration ye cɔla denitration ye cɔla denitration ye cɔla denitration ye cɔla denitration ye cɔla denitration ye cɔla denitration ye cɔla denitration ye cɔla denitration ye cɔla denitration ye cɔla denitration ye cɔla denitrat SCR ye luɔɔi de NOx ye cɔk tɔ̈ɔ̈u thïn, ku teknolojii dït apɛi ee ammonia ye cɔk tɔ̈ɔ̈u thïn. A ye gas ye NH3 (gas) tɔ̈ɔ̈u ka tɔ̈ɔ̈u ka tɔ̈ɔ̈u ka tɔ̈ɔ̈u ka tɔ̈ɔ̈u ka tɔ̈ɔ̈u ka tɔ̈ɔ̈u Në luɔɔi de catalyst, NH3 (gas) bɛ̈n ya cɔk NOx, bɛ̈n ya cɔk NOx bɛ̈n ya cɔk H2O ku N2, ku bɛ̈n ya cɔk nitrogen de ≥90%. Në ye mɛn, kä ye kek tɔ̈ɔ̈u në teknoloji kënë ye 98% ye kek tɔ̈ɔ̈u në teknoloji ye kek tɔ̈ɔ̈u në duniɛ yiic.
4. Prinsip luɔɔi
SCR technology is a reducing agent (NH3, urea) in the role of metal catalyst, selectively reacting with NOx to generate N2 and H2O, rather than being oxidized by O2, therefore called "selective". SCR technology is a reducing agent (NH3, urea) in the role of metal catalyst, selectively reacting with NOx to generate N2 and H2O, rather than being oxidized by O2, therefore called "selective". Kä ye kɛ̈n ye kɛ̈n ye kɛ̈n ye kɛ̈n ye kɛ̈n ye kɛ̈n ye kɛ̈n ye:
4NH3+4NO+O2→4N2+6H2O
4NH3+2NO2+O2→6N2+6H2O
Ni catalyst ye luɔ̈ɔ̈i bï NH3 ku NOx ya cɔk tɔ̈ɔ̈u, a tɛmɛ tɛmɛ tɛmɛ tɛmɛ tɛmɛ tɛmɛ tɛmɛ tɛmɛ tɛmɛ tɛmɛ tɛmɛ Në catalyst, TiO2 ye kɛ carrier, vanadium ye kɛ catalyst ye kɛ active ingredient ye kɛ catalyst ye kɛ catalyst ye kɛ catalyst ye kɛ catalyst ye kɛ catalyst ye kɛ catalyst ye kɛ catalyst ye kɛ catalyst ye kɛ catalyst ye kɛ catalyst ye kɛ catalyst ye kɛ catalyst ye kɛ catalyst A tɛmɛ tɛmɛ tɛmɛ tɛmɛ 300-400°C WO3 ani/wala MoO3 aye tɔ̈ɔ̈u në catalyst kɔ̈k peei yiic. A ka baara ye ka catalyst ya juak ku ka thermal stability ya juak, ka titanium ye cɔk tɔ̈ɔ̈u ka cɔk tɔ̈ɔ̈u ka cɔk tɔ̈ɔ̈u ka cɔk tɔ̈ɔ̈u.
Denitrification efficiency, 90%;
5. Features of dust removal process
Dust remover ye luɔ̈ɔ̈i ye ceramic multi-tube cyclone dust remover, bag dust remover, electrostatic dust remover, ka baara juëc ye luɔ̈ɔ̈i ye ceramic multi-tube cyclone dust remover, secondary bag dust remover, ka bɛ̈ɛ̈i bɛ̈ɛ̈i bɛ̈ɛ̈i bɛ̈ɛ̈i b
Ceramic multi-tube cyclone dust remover ye tɛmɛ tɛmɛ tɛmɛ tɛmɛ tɛmɛ tɛmɛ tɛmɛ tɛmɛ tɛmɛ tɛmɛ tɛmɛ tɛmɛ tɛmɛ tɛmɛ tɛmɛ Second-level cloth bag dust remover dust removal effect is good, and the filter mechanism of cloth bag dust remover determines that it is not affected by burning coal species materialization performance changes, having a stable dust removal efficiency. Kä ye kek tɛ̈n ye kek tɛ̈n ye kek tɛ̈n ye kek tɛ̈n ye kek tɛ̈n ye kek tɛ̈n ye kek tɛ̈n ye kek tɛ̈n ye kek tɛ̈n ye kek t Ka tɛmɛ, ka tɛmɛ ye 99.99%, ka tɛmɛ ye 50 mg/Nm3, ka tɛmɛ ye 10 mg/Nm3, ka tɛmɛ ye zero.
6. Bi-alkali Desulfurization Features
Teknoloji de sulfur de gas de fume bi-alkaline ye kä ye kek cɔl limestone-limestone ye lac looi. Calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfate, calcium sulfateSkalaA, a ye cɔl blockage phenomenon. Kä ye kek tɔ̈ɔ̈u në kë de kä ye kek tɔ̈ɔ̈u në kë de kä ye kek tɔ̈ɔ̈u në kë de kä ye kek tɔ̈ɔ̈u në kë de kä ye kek tɔ̈ɔ̈u në kë de kä ye kek Walasa ka tɛmɛ calcium-based desulfurizers, calcium-based desulfurizers, ka tɛmɛ calcium-based desulfurizers, ka tɛmɛ calcium-based desulfurizers, ka tɛmɛ calcium-based desulfurizers, ka tɛmɛ calcium-based desulfurizers, ka tɛmɛ calcium-based desulfurizers.SkalaKɔnɔŋ ye kɔnɔŋ ye kɔnɔŋ ye kɔnɔŋ ye kɔnɔŋ ye kɔnɔŋ ye kɔnɔŋ ye kɔnɔŋ ye kɔnɔŋ ye kɔnɔŋ ye kɔnɔŋ ye kɔnɔŋ ye kɔnɔŋ ye kɔnɔŋ ye kɔnɔŋ ye kɔnɔŋ ye kɔnɔŋ
Ka tɛmɛ kek limestone wala limestone wet method de desulfurization, dual alkali method ee kä ye kek looi: 1, NaOH desulfurization, circulating water is essentially NaOH's water solution, in the circulation process for water pumps, pipelines, equipment no corrosion and blockage phenomenon, facilitating equipment operation and maintenance.
2, absorbent regeneration and desulfurization sludge precipitation occurs outside the tower, so avoiding inside the tower blockage and wear, enhancing the reliability of operation, reducing operating costs. 2, absorbent regeneration and desulfurization sludge precipitation occurs outside the tower, so avoiding inside the tower blockage and wear, enhancing the reliability of operation, reducing operating costs. A bɛ se ka tɔ̈ɔ̈u ka tɔ̈ɔ̈u ka tɔ̈ɔ̈u ka tɔ̈ɔ̈u ka tɔ̈ɔ̈u ka tɔ̈ɔ̈u ka tɔ̈ɔ̈u ka tɔ̈ɔ̈u ka tɔ̈ɔ̈u ka t
3, sodium-based absorbing liquid absorbs SO2 quickly, so can be used a small liquid gas ratio, to achieve a high desulfurization efficiency, generally at more than 90%; 3, sodium-based absorbing liquid absorbs SO2 quickly, so can be used a small liquid gas ratio, to achieve a high desulfurization efficiency, generally at more than 90%; 3, sodium-based absorbing liquid absorbs SO2 quickly
4, në luɔɔi de luɔɔi de luɔɔi de luɔɔi de luɔɔi de luɔɔi de luɔɔi de luɔɔi de luɔɔi de luɔɔi de luɔɔi de luɔɔi de luɔɔi de luɔɔi
Na2SO4, NaSO3 oxidation side reaction, Na2SO4, Na2CO3, NaOH, Na2CO3, Na2SO4, Na2SO4, Na2SO4, Na2SO4, Na2SO4, Na2CO3, Na2CO3, Na2CO3, Na2CO3, Na2CO3, Na2CO3 Na2SO4 bɛ̈n ya tɔ̈ɔ̈u bɛ̈n ya tɔ̈ɔ̈u bɛ̈n ya tɔ̈ɔ̈u bɛ̈n ya tɔ̈ɔ̈u.
Teknoloji de sulfur de bialkali ye teknoloji ye kɔc cɔl sulfur de gas de coke ye kɔc cɔl sulfur de gas de coke ye kɔc cɔl sulfur de gas de coke ye kɔc cɔl sulfur de gas de coke ye kɔc cɔl sulfur de gas de coke ye kɔc cɔl sulfur de gas de coke
7. Ammonium-sulfur ammonium desulfurization process characteristics
Ammoniak de sulfur ye looi në yemɛɛn, ye looi në luɔɔi de sulfur ye looi në luɔɔi de sulfur ye looi në luɔɔi de sulfur ye looi në luɔɔi de sulfur ye looi në luɔɔi de sulfur ye looi në luɔɔi de sulfur ye looi në luɔɔi de sulfur ye looi në luɔɔi de sulfur ye looi në luɔɔi de sulfur ye looi në luɔɔi de sulfur ye looi në luɔɔi de sulfur ye loo
1, luɔɔi dɔ̈ŋ, ka tɛ̈n tɔ̈u sulfur content, boiler capacity. Ni sulfur ye kɔnɔ, ammonium sulfate ye kɔnɔ.
2, sulfur de-tɛ-tɛ-tɛ-tɛ-tɛ-tɛ-tɛ-tɛ-tɛ-tɛ-tɛ-tɛ-tɛ-tɛ-tɛ-tɛ Ka tɔ̈u yen, ka tɔ̈u yen, ka tɔ̈u yen, ka tɔ̈u yen, ka tɔ̈u yen, ka tɔ̈u yen, ka tɔ̈u yen, ka tɔ̈u yen, ka tɔ̈u yen, ka tɔ̈u yen.
3, ye kä ye kɔɔr ye kɔɔr ye kɔɔr ye kɔɔr ye kɔɔr ye kɔɔr ye kɔɔr ye kɔɔr ye kɔɔr ye kɔɔr ye kɔɔr ye kɔɔr ye kɔɔr ye kɔɔr ye kɔɔr
4, ammonia method desulfurization device has a strong adaptability to unit load changes, can adapt to fast start, cold state start, temperature state start, hot state start and other ways. 4, ammonia method desulfurization device has a strong adaptability to unit load changes, can adapt to fast start, cold state start, temperature state start, hot state start and other ways. Ajuiɛɛr ye luui në 35% BMCR ~ 140% BMCR.
5, tɛ̈n tɛ̈n tɛ̈n tɛ̈n tɛ̈n tɛ̈n tɛ̈n tɛ̈n tɛ̈n tɛ̈n tɛ̈n tɛ̈n tɛ̈n t
6, ammonia ye alkaline absorbent ye, absorbent ye luɔɔi ye dɔɔni.
7. Ammoniak sulfate ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ ye kɔnɔ
Denitrification dust removal desulfurization integrated design process: fume gas → compressed fan → residual heat recovery device (coal saver) → heat exchanger → desulfurization dust removal integrated tower → heat exchanger → high air emission.
8. Sulfur de dust removal system selection description
Sisitɛm kënë adhil bï ya looi në kë de boiler model, coal burning, smoke gas composition, smoke gas flow, temperature, media concentration and other indicators and user requirements, can undertake all or part of the projects, our company has a special calculation program software, ensuring selection is accurate and reasonable.
9. Wɛɛr de luɔi
Sisitɛm kënë ee luɔ̈ɔ̈i në luɔɔi de wɛ̈ɛ̈r, luɔɔi de wɛ̈ɛ̈r, luɔɔi de wɛ̈ɛ̈r, luɔɔi de wɛ̈ɛ̈r, luɔɔi de simɛnti, luɔɔi de wɛ̈ɛ̈r, luɔɔi de wɛ̈ɛ̈r, luɔɔi de wɛ̈ɛ̈r, luɔɔi
