阅读说明：本技术 一种煤气羰基硫脱除药剂 (Gas carbonyl sulfide removal agent ) 是由 许传东 于 2020-11-13 设计创作，主要内容包括：本发明公开了一种煤气羰基硫脱除药剂,包括氧化剂和稳定剂,其中,稳定剂包括络合铁和铁无机盐,氧化剂包括双氧水、次氯酸钠和高锰酸钾。在使用本发明公开的煤气羰基硫脱除药剂时,将其于TRT后通过喷雾或鼓泡的方式加入反应器中,进行羰基硫的脱除。本发明公开的煤气羰基硫脱除药剂,可以选择性氧化煤气中羰基硫和硫化氢成分,而不与煤气中的一氧化碳和二氧化碳及氢反应,将羰基硫和硫化氢氧化成二氧化硫及三氧化硫,经碱性溶液氢氧化钠吸收转化为硫酸钠,羰基硫脱除效率高,能够有效适应煤气中羰基硫和硫化氢含量变化,减少药剂消耗量及废水排放量。经过实际试验,能够将羰基硫脱除系统整体运行成本降低70％,并且后期维护简单。(The invention discloses a gas carbonyl sulfide removal agent, which comprises an oxidant and a stabilizer, wherein the stabilizer comprises complex iron and iron inorganic salt, and the oxidant comprises hydrogen peroxide, sodium hypochlorite and potassium permanganate. When the gas carbonyl sulfide removal agent disclosed by the invention is used, the gas carbonyl sulfide removal agent is added into a reactor after TRT in a spraying or bubbling mode to remove carbonyl sulfide. The gas carbonyl sulfide removal agent disclosed by the invention can selectively oxidize carbonyl sulfide and hydrogen sulfide components in gas without reacting with carbon monoxide, carbon dioxide and hydrogen in the gas, the carbonyl sulfide and the hydrogen sulfide are oxidized into sulfur dioxide and sulfur trioxide, and the sulfur dioxide and the sulfur trioxide are absorbed and converted into sodium sulfate by alkaline solution sodium hydroxide, so that the carbonyl sulfide removal efficiency is high, the gas carbonyl sulfide removal agent can effectively adapt to the content change of the carbonyl sulfide and the hydrogen sulfide in the gas, and the agent consumption and the wastewater discharge are reduced. Through practical tests, the overall operation cost of the carbonyl sulfide removal system can be reduced by 70%, and the later maintenance is simple.)

1. The gas carbonyl sulfide removal agent is characterized by comprising an oxidizing agent and a stabilizing agent, wherein the stabilizing agent comprises complex iron and iron inorganic salt.

2. The gas carbonyl sulfide removal agent as claimed in claim 1, wherein said agent comprises an oxidant and a stabilizer, wherein the complex iron in said stabilizer is one or more of ferric citrate, Fe (EDTA) and Fe (TEA).

3. The gas carbonyl sulfide removal agent as claimed in claim 1, wherein the agent comprises an oxidant and a stabilizer, wherein the iron inorganic salt in the stabilizer is one or more of ferric nitrate, ferric sulfate and ferrous sulfate.

4. The gas carbonyl sulfide removal agent as claimed in claim 1, wherein the oxidant comprises hydrogen peroxide, sodium hypochlorite and potassium permanganate.

5. The gas carbonyl sulfide removal agent as claimed in claim 1, wherein the mass concentration of the complexed iron in the stabilizer is 1.6-4.3%, and the mass concentration of the iron inorganic salt is 0.2-1.2%.

6. The gas carbonyl sulfide removal agent as claimed in claim 4, wherein in the oxidant, the mass concentration of hydrogen peroxide is 2-15%, the mass concentration of sodium hypochlorite is 4-20%, and the mass concentration of potassium permanganate is 0.5-6%.

7. The gas carbonyl sulfide removal agent as claimed in claim 1, wherein the oxidant and the stabilizer are respectively prepared at normal temperature, stored in 316L stainless steel storage tanks, and mixed according to a volume ratio of 1:1 for use.

8. The use method of the gas carbonyl sulfide removal agent as claimed in any one of claims 1 to 7, wherein the gas carbonyl sulfide removal agent is added into the reactor after TRT to remove carbonyl sulfide.

9. The use method of a gas carbonyl sulfide removal agent as claimed in claim 8, wherein the feeding mode into the reactor is nozzle injection or bubbling device bubbling.

Technical Field

The application relates to a coal gas treatment process, in particular to a coal gas carbonyl sulfide removal agent and a process for oxidizing and absorbing carbonyl sulfide by using the agent.

Background

Carbonyl sulfide (COS) widely exists in important industrial gases related to coal chemical industry and petrochemical industry, such as coke oven gas, water gas, natural gas, liquefied petroleum gas and Claus tail gas, and is generally associated with other sulfur compounds such as H₂S, etc. are present at the same time. Sulfides can cause equipment corrosion and catalyst poisoning during production. In addition, COS that is released to the atmosphere without treatment can form SO₂Promoting photochemical reactions, which poses serious environmental problems. Therefore, in industries such as coal chemical industry, COS needs to be removed.

COS is difficult to remove by adopting a conventional method, and the current main removal technologies comprise an organic amine absorption method, a hydro-conversion method, a catalytic hydrolysis method, an oxidation conversion method and the like.

At present, the carbonyl sulfide removal of a steel mill mainly adopts a catalytic hydrolysis process, an alumina catalyst is mostly adopted, heavy metal components are contained in the components, the components are influenced by hydrogen chloride in blast furnace gas and react with the hydrogen chloride in the gas to produce chloride, so that the catalyst fails, and the catalyst is of a honeycomb structure, has large floor area and large gas resistance, and does not meet the requirements of energy conservation and environmental protection. Meanwhile, the process has the advantages of high investment cost, easy catalyst poisoning, high replacement cost, complex catalyst components after removal treatment, belonging to dangerous waste, high treatment difficulty and easy secondary pollution. The product after the catalytic hydrolysis process is desulfurized is sodium sulfide which is unstable and is easy to decompose to separate out hydrogen sulfide again, so that secondary pollution and personnel poisoning risks are caused. Based on the wet oxidation principle and the background of removing hydrogen sulfide by complexing iron, the invention provides a method for removing COS in the coal chemical industry by coupling by using hydrogen peroxide, sodium hypochlorite and potassium permanganate as oxidants and complexing iron and iron inorganic salts as stable removal agents so as to realize the high-efficiency removal of gas carbonyl sulfide.

Disclosure of Invention

The invention provides a gas carbonyl sulfide removal agent and a process for oxidizing and absorbing carbonyl sulfide by using the agent, aiming at the problems of high investment cost, high operating cost, unstable removal efficiency and secondary pollution of the existing domestic gas carbonyl sulfide removal process. The process can greatly reduce the investment cost and the operation cost of the existing gas carbonyl sulfide removal process, the investment cost and the operation cost are 30 percent of those of the catalytic hydrolysis process, and the problem of secondary pollution is avoided.

The purpose of the invention is realized by the following technical scheme.

A coal gas carbonyl sulfide removal agent comprises an oxidizing agent and a stabilizing agent, wherein the stabilizing agent comprises complex iron and an iron inorganic salt, and the complex iron is one or more of ferric citrate, Fe (EDTA) and Fe (TEA); the iron inorganic salt is one or more of ferric nitrate, ferric sulfate and ferrous sulfate.

Preferably, the oxidant comprises hydrogen peroxide, sodium hypochlorite and potassium permanganate.

Preferably, in the stabilizer, the mass concentration of the complex iron is 1.6-4.3%, and the mass concentration of the iron inorganic salt is 0.2-1.2%.

Preferably, in the oxidant, the mass concentration of the hydrogen peroxide is 2-15%, the mass concentration of the sodium hypochlorite is 4-20%, and the mass concentration of the potassium permanganate is 0.5-6%.

Preferably, the oxidant and the stabilizer are respectively configured at normal temperature, are respectively stored in 316L stainless steel storage tanks, and are mixed according to a volume ratio of 1:1 for use.

On the other hand, the invention also provides a using method of the coal gas carbonyl sulfide removal agent, and specifically, the coal gas carbonyl sulfide removal agent is added into the reactor after TRT to remove carbonyl sulfide.

Preferably, the feeding means is a nozzle or a bubbling device.

The invention discloses a gas carbonyl sulfide removal agent, which is characterized in that a certain stabilizer is added on the basis of a traditional oxidant to selectively oxidize carbonyl sulfide and hydrogen sulfide components in gas without reacting with carbon monoxide, carbon dioxide and hydrogen in the gas, the carbonyl sulfide and the hydrogen sulfide are oxidized into sulfur dioxide and sulfur trioxide, the sulfur dioxide and the sulfur trioxide are absorbed by alkaline solution sodium hydroxide and converted into sodium sulfate, and sodium sulfate water mist particles are removed by a demister to obtain dry and clean gas.

The invention discloses a gas carbonyl sulfide removal agent, which is a SACSR carbonyl sulfide removal agent containing an oxidant and a stabilizer and can simultaneously remove COS and CS in gas according to the characteristics of the gas₂And H₂S is oxidized into sulfate ions, and then the sulfate ions are absorbed by sodium hydroxide solution and converted into sodium sulfate, and the sulfur-containing wastewater is removed by a rear-end water removal device, so that the aim of fine desulfurization of coal gas is fulfilled. According to the experimental result, the total sulfur in the coal gas can be reduced to 6% of the original mass concentration by adopting a 3-stage bubbling device, and the aim of fine desulfurization of the coal gas is fulfilled. In Shanxi Jianbang iron and steel, a two-stage spraying mode is adopted to mix carbonyl sulfide medicament and sodium hydroxide solution to be thickly sprayed, and the carbonyl sulfide medicament and the sodium hydroxide solution can be sprayedCan lead carbonyl sulfur to be 70mg/Nm from the original concentration³Down to 10mg/Nm³(ii) a Simultaneously, hydrogen sulfide in the coal gas is removed, so that the effects of one-time investment and removal of hydrogen sulfide and carbonyl sulfide are achieved.

The gas carbonyl sulfide removal agent disclosed by the invention can effectively reduce the investment cost of equipment for gas fine desulfurization, the investment amount is 30% of that of a catalytic hydrolysis process, and meanwhile, the operation cost can be effectively reduced. The reagent is sprayed into the reactor after TRT, redundant moisture is removed through the demisting tower, pressure loss to the original gas pipeline system is small, simultaneously the removal efficiency is high, the reagent can effectively adapt to the content change of carbonyl sulfide and hydrogen sulfide in the gas, and the reagent consumption and the wastewater discharge are reduced. Through practical tests, the coal gas carbonyl sulfide removal agent disclosed by the invention can reduce the overall operation cost of a carbonyl sulfide removal system by 70%, and is simple in later maintenance.

Detailed Description

The following are specific embodiments of the present invention for the purpose of illustration and description.

Example 1

A gas carbonyl sulfide removal agent comprises an oxidant and a stabilizer, wherein the oxidant comprises hydrogen peroxide, sodium hypochlorite and potassium permanganate, and the stabilizer comprises complex iron and iron inorganic salt.

Preparing composite oxidants of 5%, 8% and 3% of hydrogen peroxide, sodium hypochlorite and potassium permanganate respectively at normal temperature, and storing in a 316L stainless steel storage tank for later use; at normal temperature, 3% and 0.5% of stabilizers of Fe (EDTA) and ferric nitrate respectively are prepared and stored in a 316L stainless steel storage tank for later use.

And a three-stage bubbling device is arranged behind a TRT (blast furnace gas excess pressure turbine power generation device), and the gas carbonyl sulfide removing agent mixed according to the volume ratio of 1:1 of the oxidant to the stabilizer is sprayed into the gas to remove organic sulfur such as COS and the like in the gas. Tests show that the total sulfur in the coal gas is reduced to 6% of the original concentration, and the aim of fine desulfurization of the coal gas is achieved.

Example 2

A gas carbonyl sulfide removal agent comprises an oxidant and a stabilizer, wherein the oxidant comprises hydrogen peroxide, sodium hypochlorite and potassium permanganate, and the stabilizer comprises complex iron and iron inorganic salt.

Preparing 15%, 4% and 0.5% composite oxidants of hydrogen peroxide, sodium hypochlorite and potassium permanganate at normal temperature, and storing in a 316L stainless steel storage tank for later use; at normal temperature, stabilizers of ferric citrate, Fe (EDTA) and ferric sulfate with mass fractions of 1.8%, 1.2% and 0.5% are prepared and stored in a 316L stainless steel storage tank for later use.

A two-stage spraying device is arranged behind a blast furnace gas residual pressure turbine power generation device TRT, and the gas carbonyl sulfide removing agent mixed according to the volume ratio of 1:1 of an oxidant and a stabilizer is sprayed into gas to remove organic sulfur such as COS and the like in the gas. It was tested that the carbonyl sulfide concentration was 70mg/Nm from the original concentration³Down to 10mg/Nm³And simultaneously removing hydrogen sulfide from the coal gas.

Example 3

A gas carbonyl sulfide removal agent comprises an oxidant and a stabilizer, wherein the oxidant comprises hydrogen peroxide, sodium hypochlorite and potassium permanganate, and the stabilizer comprises complex iron and iron inorganic salt.

Preparing composite oxidants of hydrogen peroxide, sodium hypochlorite and potassium permanganate with the mass fractions of 2%, 20% and 6% respectively at normal temperature, and storing the composite oxidants in a 316L stainless steel storage tank for later use; fe (TEA) and stabilizers with a mass fraction of ferric nitrate and ferrous sulfate of 1.6%, 0.6% and 0.6%, respectively, were stored in a 316L stainless steel storage tank for further use.

A two-stage spraying device is arranged behind a blast furnace gas residual pressure turbine power generation device TRT, and the gas carbonyl sulfide removing agent mixed according to the volume ratio of 1:1 of an oxidant and a stabilizer is sprayed into gas to remove organic sulfur such as COS and the like in the gas. Carbonyl sulfide was tested at a concentration of 82mg/Nm from the original concentration³Down to 14mg/Nm³And simultaneously removing hydrogen sulfide from the coal gas.

Example 4

A gas carbonyl sulfide removal agent comprises an oxidant and a stabilizer, wherein the oxidant comprises hydrogen peroxide, sodium hypochlorite and potassium permanganate, and the stabilizer comprises complex iron and iron inorganic salt.

Preparing composite oxidants of 8%, 4% and 3% of hydrogen peroxide, sodium hypochlorite and potassium permanganate respectively at normal temperature, and storing in a 316L stainless steel storage tank for later use; fe (TEA) and ferric sulfate iron mass fractions were 1.6% and 1.2% respectively of the stabilizer and stored in 316L stainless steel storage tanks for later use.

A two-stage spraying device is arranged behind a blast furnace gas residual pressure turbine power generation device TRT, and the gas carbonyl sulfide removing agent mixed according to the volume ratio of 1:1 of an oxidant and a stabilizer is sprayed into gas to remove organic sulfur such as COS and the like in the gas. Carbonyl sulfide was tested at a concentration of 82mg/Nm from the original concentration³Down to 11mg/Nm³And simultaneously removing hydrogen sulfide from the coal gas.

Example 5

A gas carbonyl sulfide removal agent comprises an oxidant and a stabilizer, wherein the oxidant comprises hydrogen peroxide, sodium hypochlorite and potassium permanganate, and the stabilizer comprises complex iron and iron inorganic salt.

Preparing 15%, 4% and 0.5% composite oxidants of hydrogen peroxide, sodium hypochlorite and potassium permanganate at normal temperature, and storing in a 316L stainless steel storage tank for later use; at normal temperature, 3% and 0.5% of stabilizing agents of ferric citrate and ferric nitrate by mass fraction are prepared and stored in a 316L stainless steel storage tank for later use.

A two-stage spraying device is arranged behind a blast furnace gas residual pressure turbine power generation device TRT, and the gas carbonyl sulfide removing agent mixed according to the volume ratio of 1:1 of an oxidant and a stabilizer is sprayed into gas to remove organic sulfur such as COS and the like in the gas. The tested carbonyl sulfide concentration is 94mg/Nm from the original concentration³Down to 15mg/Nm³。

Example 6

A gas carbonyl sulfide removal agent comprises an oxidant and a stabilizer, wherein the oxidant comprises hydrogen peroxide, sodium hypochlorite and potassium permanganate, and the stabilizer comprises complex iron and iron inorganic salt.

Preparing composite oxidants of hydrogen peroxide, sodium hypochlorite and potassium permanganate with the mass fractions of 11%, 13% and 2% respectively at normal temperature, and storing the composite oxidants in a 316L stainless steel storage tank for later use; at normal temperature, stabilizers with the mass fractions of Fe (TEA) and ferric nitrate of 4.3% and 2% respectively were prepared and stored in a 316L stainless steel storage tank for further use.

And a three-stage bubbling device is arranged behind a TRT (blast furnace gas excess pressure turbine power generation device), and the gas carbonyl sulfide removing agent mixed according to the volume ratio of 1:1 of an oxidant and a stabilizer is bubbled into the gas to remove organic sulfur such as COS and the like in the gas. Carbonyl sulfide was tested at a concentration of 103mg/Nm from the original concentration³Down to 19mg/Nm³And simultaneously removing hydrogen sulfide from the coal gas.