Process for producing sodium hydroxymethyl sulfonate by using byproduct formaldehyde and sodium sulfate

A technology of sodium hydroxymethanesulfonate and by-product sodium sulfate, which is applied in the fields of sulfonate preparation and organic chemistry, and can solve the problems of high calorie and manpower, limited demand for sodium sulfide, and difficulty in marketing

Active Publication Date: 2022-07-05
CHONGQING KOOPPER CHEM IND
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In addition, in the chemical industry, the formaldehyde gas produced by the depolymerization of paraformaldehyde participates in the reaction. Because it cannot be fully utilized, there is a certain loss and the production cost is high. At the same time, the formaldehyde gas is discharged through the tail gas, causing pollution to the environment and facing great environmental protection risks. , using the incineration law to invest a lot, it is unbearable for small enterprises
[0003] With the development of society, people have higher and higher requirements for environmental protection, and the sewage treatment must meet the discharge standards. However, the sulfuric acid or sodium sulfate exceeding the standard in the production wastewater has brought huge pressure to the sewage treatment, and even affected the normal production of the company.
There are many sources of sodium sulfate in the society, which has become a difficult problem to deal with, and even some sodium sulfate solids that cannot be processed normally have become new wastes, causing serious pollution to the environment
The current main destinations of sodium sulfate produced in the enterprise are as follows: 1. Dehydration to make sodium sulfate containing water, which is handed over to sodium sulfide manufacturers to make sodium sulfide, but the demand for sodium sulfide is limited and the value of sodium sulfide is not high
2. Concentration, crystallization, recrystallization, drying and dehydration to obtain anhydrous sodium sulfate as a dry reagent requires a lot of heat, extra manpower and equipment, and anhydrous sodium sulfate is cheap and difficult to promote in the market
3. Handed over to environmental protection enterprises as hazardous waste treatment, environmental protection enterprises can only be treated as hazardous waste through incineration and burial, but failed to cure, and there is still secondary pollution to the environment
4. There are a small number of enterprises that make sodium sulfate solution into sodium bisulfite, which can also produce certain benefits. However, the production equipment and production technology are not mature enough to produce on a large scale

Method used

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  • Process for producing sodium hydroxymethyl sulfonate by using byproduct formaldehyde and sodium sulfate
  • Process for producing sodium hydroxymethyl sulfonate by using byproduct formaldehyde and sodium sulfate
  • Process for producing sodium hydroxymethyl sulfonate by using byproduct formaldehyde and sodium sulfate

Examples

Experimental program
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Effect test

Embodiment 1

[0035] like figure 1Shown, a kind of technology that utilizes by-product formaldehyde and sodium sulfate to produce sodium hydroxymethanesulfonate, comprises the steps:

[0036] Step 1, 4000kg concentration is that the by-product sodium sulfate solution of 20% is added in the reactor, then adds organic matter in the toluene extraction solution, and the addition of toluene is 500L; The purpose of toluene addition is: remove the by-product sodium sulfate solution Organic impurities to ensure that the color of the product is qualified;

[0037] Step 2, add 487kg technical grade (90%) calcium hydroxide (solid) in the reaction kettle, turn on the forced circulation pump and heat the reaction kettle to 50-55 ℃, pass into sulfur dioxide gas after 30min and carry out spray absorption;

[0038] Step 3. Through on-line sulfate and calcium ion detection, when the sulfate ion concentration is lower than 0.2%, the method of recalling sodium sulfate and (or) introducing sulfur dioxide ensu...

Embodiment 2

[0044] Embodiment 2 Solvent, activated carbon cycle apply mechanically

[0045] Step 1, adding 4000kg of by-product sodium sulfate solution with a concentration of 30% into the reactor, then adding 500L of toluene to extract the organic matter in the solution;

[0046] Step 2, add 731kg technical grade (90%) calcium hydroxide (solid) in the reaction kettle, turn on the forced circulation pump and heat the reaction kettle to 50-55 ℃, pass into sulfur dioxide gas after 30min and carry out jet absorption;

[0047] Step 3: Real-time detection of the sodium sulfate concentration by the online detection system, by adjusting the sodium sulfate and feeding the sulfur dioxide to ensure that the sodium sulfate concentration is less than 0.2% and the calcium ion concentration is less than 0.4%, and then the reaction solution is transferred to the plate and frame filter press The solid-liquid separation is carried out in the machine, the filtrate is sucked into the concentration kettle by...

Embodiment 3

[0053] The mechanical application of embodiment 3 sulfurous acid

[0054] combine figure 2 As shown, step 1, 4000kg concentration is that the by-product sodium sulfate solution of 20% is added in the reactor, then adds organic matter in the toluene extraction solution, the addition of toluene is 500L, then transfers into (secondary or three) by pump grade) in the sulfur dioxide tail gas absorption kettle;

[0055] Step 2, add 487kg industrial grade (90%) calcium hydroxide (solid) to the (second or third) sulfur dioxide tail gas absorption kettle, turn on the forced circulation pump and heat it to 50-55 ° C, spray and absorb the overflowing sulfur dioxide gas of the upper stage ;

[0056] Step 3: When the reaction in the upper-level reactor is complete, the reaction solution is processed and the materials (sodium sulfate solution, solid calcium hydroxide) are added again, and the tail gas is absorbed as a three-level absorption tank. Sulfur dioxide gas is introduced into th...

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PUM

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Abstract

The invention relates to the technical field of preparation of sodium hydroxymethyl sulfonate, and discloses a process for producing sodium hydroxymethyl sulfonate by using byproducts formaldehyde and sodium sulfate, which comprises the following steps: step 1, adding a toluene solution into a byproduct sodium sulfate solution to extract organic impurities; step 2, adding calcium hydroxide into the sodium sulfate solution subjected to impurity removal, and reacting to obtain sodium hydrogen sulfite; 3, filtering the reaction liquid in the step 2 to obtain a solid phase and filtrate, and drying the solid phase to obtain gypsum powder; 4, concentrating the filtrate to obtain a saturated sodium hydrogen sulfite solution; and 5, reacting the saturated sodium hydrogen sulfite solution with the byproduct formaldehyde solution to obtain the sodium hydroxymethyl sulfonate. According to the invention, the byproduct sodium sulfate is prepared into sodium hydrogen sulfite by using a simpler, more mature and brand-new production process, then the sodium hydrogen sulfite reacts with the byproduct formaldehyde, and the sodium hydroxymethyl sulfonate which is high in value, wide in applicability and large in market demand is prepared through deep processing, so that a new way for synthesizing the sodium hydroxymethyl sulfonate is provided, and the recycling of chemical byproducts is realized.

Description

technical field [0001] The invention relates to the technical field of preparation of sodium hydroxymethanesulfonate, in particular to a process for producing sodium hydroxymethanesulfonate by utilizing by-product formaldehyde and sodium sulfate. Background technique [0002] Sodium hydroxymethanesulfonate is used as an intermediate for sodium isoniazid sulfonate, neoarsinvaramine, carcinogen, etc. It is also used as a fixative for protein flavor, a floating lotion for lead-zinc ore and a color photo assistant ( Anti-pollution and fading) and cotton printing industry, the market demand is large, and the price is not cheap. At present, the existing processing method of sodium hydroxymethanesulfonate mainly utilizes the addition of formaldehyde and sodium bisulfite at 60 to 65°C. In addition, the depolymerization of paraformaldehyde in the chemical industry produces formaldehyde gas to participate in the reaction. Since it cannot be fully utilized, certain losses occur and th...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C303/32C07C309/08
CPCC07C303/32C01D5/145C07C309/08
Inventor 沈寒冰刘业红曾浩杨福平余支明潘玮王天宇
Owner CHONGQING KOOPPER CHEM IND
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