Method for direct conversion of plant soapstock into fatty acid

A technology of fatty acid and soapstock, which is applied in the field of direct conversion of vegetable soapstock into fatty acid, can solve the problems of large energy consumption and acid consumption, a large amount of waste water and waste gas, etc., and achieves simple process operation, large device processing capacity, and low sulfuric acid consumption. Effect

Inactive Publication Date: 2016-07-13
九江力山环保科技有限公司
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Problems solved by technology

[0003] The purpose of the present invention is to provide a method for directly converting plant soapstock into fatty acid, which solves the technical problems of high energy consumption, large amount of acid, generation of a large amount of waste water and waste gas, and serious environmental pollution in the fatty acid production process. Easy to operate, full reaction between plant soapstock and sulfuric acid, less sulfuric acid consumption, thorough acidification and direct generation of fatty acids, large processing capacity, stable quality, odorless, low energy consumption, low cost, no waste water generation, energy saving and environmental protection

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  • Method for direct conversion of plant soapstock into fatty acid

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Embodiment Construction

[0015] This method, such as figure 1 shown, including the following steps:

[0016] 1) The plant soapstock raw material in the raw material tank 6 is transported to the preheater 1 by the gear pump 7 at a flow rate of 9000Kg / h and heated to 70~80°C;

[0017] 2) After the plant soapstock raw material is heated by the preheater 1, it is transported to the high-speed stirring reactor 2, and under the high-speed stirring at a speed of 1200 rpm, it fully contacts and reacts with sulfuric acid, and the reaction temperature is controlled at 105-115°C. After the discharge, the fatty acid hydrolysis rate has reached more than 94%, wherein the sulfuric acid is uniformly and quantitatively input from the sulfuric acid storage tank 12 with the flow rate of 200Kg / h by the metering pump 8, and the raw material ratio of sulfuric acid and plant soapstock is 2:90;

[0018] 3) The mixed solution of plant soapstock raw material and sulfuric acid in the high-speed stirring reactor 2 after stirri...

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Abstract

The invention relates to a method for direct conversion of plant soapstock into fatty acid. The method includes: heating plant soapstock by a preheater and conveying it into a high-speed stirring reactor, and fully stirring the plant soapstock with quantitative sulfuric acid, then conducting secondary mixing through a static mixer, then carrying out stirring reaction in a reaction kettle, then performing deslagging and dehydration through a reaction precipitation tank to obtain high yield fatty acid. And the discharged water is returned to a raw material tank to carry out acid-base reaction with plant soapstock raw material, and part of the generated fatty acid enters the next cycle. The invention is a new approach for direct generation of fatty acid by continuous acidification of plant soapstock, and avoids the procedure of producing soapstock into acid oil and then performing hydrolysis. The method provided by the invention has the characteristics of easy technological operation, complete reaction of plant soapstock and sulfuric acid, small sulfuric acid dosage, thorough acidification and direct generation of fatty acid, large device treatment capacity, stable quality, no odor, low energy consumption, low cost, no wastewater production, and energy saving and environmental protection.

Description

technical field [0001] The invention relates to a method for directly converting plant soapstock into fatty acids. Background technique [0002] Vegetable oil foot is the main raw material for domestic production of fatty acid series products. At present, domestic soapstock basically uses soapstock to enter the acidification tank, add 8-10% sulfuric acid, and then heat and stir with steam to carry out acidification reaction, drain the waste water after precipitation, and obtain acidified oil, which then enters the hydrolysis tower for heating , pressurized, and hydrolyzed with water to obtain fatty acids. The process consumes a lot of energy and acid, and produces a large amount of waste water. During the acidification production process, the odor is mostly discharged in an unorganized manner, and the environmental pollution is very serious. The acidified oil produced needs to be hydrolyzed for the second time. The amount of water added is 30%, and it is heated. Temperatur...

Claims

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Application Information

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IPC IPC(8): C11B13/02C11C3/00
CPCY02W30/74C11B13/02C11C3/00
Inventor 吴中将周其飞陈飞
Owner 九江力山环保科技有限公司
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