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Device for continuously producing acidified oil and co-producing sodium sulfate crystal from nigre

A technology of sodium sulfate and acidified oil, applied in the field of soapstock processing, can solve the problems of large amount of waste water, inability to operate continuously, low soapstock conversion rate, etc., and achieve the effect of reducing pollution

Pending Publication Date: 2019-05-14
山东格瑞材料科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The purpose of the present invention is to propose a method for continuously producing acidified oil and by-product sodium sulfate crystals from soapstock, aiming at defects such as the large amount of waste water produced by the existing soapstock preparation device and process, the inability to operate continuously, and the low conversion rate of soapstock. The device realizes the continuous recycling of acid liquid, basically produces acid-containing wastewater, obtains acidified oil with a high conversion rate and at the same time obtains sodium sulfate as a by-product, and combined with the circulation of de-acidified oil, reduces the reaction temperature of raw materials and improves Raw material reaction conversion rate
[0006] It can be seen that the device of the present invention solves the problem of discharge of acidic waste water in the process of preparing acidified oil from soapstock through the design of the acid liquid circulation unit: after the reaction raw materials are acidified in the reactor, the oily reaction product in the upper layer is discharged through the upper layer. The feed port enters the settling tank for sedimentation and stratification. Because the sulfuric acid and soapstock raw materials are continuously mixed and reacted in the reactor, the upper mixed solution contains most of the oily acidified oil and part of the aqueous acid solution. After sedimentation and stratification in the settling tank, the lower layer of aqueous acid in the settling tank is re-entered into the reactor through the acid circulation unit connected to the settling tank, thereby establishing the first acid circulation loop; this acid circulation The recycling and repeated use of the acid solution in the preparation process is solved by using the circuit, so as to finally consume the acid solution in the water phase, improve the utilization rate of the acid solution and avoid the discharge of waste acid water, and do not need to set up an acid water neutralization device and sewage treatment device, reducing the environmental pollution of the process

Method used

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  • Device for continuously producing acidified oil and co-producing sodium sulfate crystal from nigre

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Effect test

Embodiment 1

[0045] A device for the continuous production of acidified oil and by-product sodium sulfate crystals from soapstock, such as figure 1 As shown, it includes a vacuum system 1, a negative pressure storage tank 2, a suction filter tank 3, a reactor 4, a settling tank 5, a buffer tank 6, a circulating oil tank 7, an acid circulation pump 8, a heater 9, and a circulation Oil pump 10, acidizing oil tank 11, raw material pump 12, raw material tank 13, acid distribution tank 14, acid discharge pump 15; reactor 4 is a raw material reactor, and is provided with an acid liquid inlet, a soapstock inlet, an upper outlet Feed port and lower discharge port; Raw material tank 13 is used for storing reaction raw material soapstock, and raw material tank 13 is connected to heater 9 through raw material pump 12, and heater 9 is connected with the soapstock inlet of reactor 4, to the raw material The soapstock is sent to the bottom of the reactor 4 after heating; the upper discharge port and the...

Embodiment 2

[0047] A kind of technique of continuously producing acidified oil and by-product sodium sulfate crystal by soapstock, it utilizes the device of embodiment 1, and technological process is as follows:

[0048] a) Aqueous sulfuric acid is added in the reactor 4; the soapstock in the raw material tank 13 enters the heater 9 through the raw material pump 12, and enters the bottom of the reactor 4 through the soapstock feeding port after being heated by the heater 9; During the process of floating from the bottom to the upper layer, it fully contacts and reacts with the acid liquid, and the acidified oil and part of the acid liquid in the upper layer of the reactor 4 enter the settling tank 5 through the upper outlet of the reactor 4 for sedimentation;

[0049] b) The acidified oil in the upper layer of the settling tank 5 reaches the overflow port and then overflows to the acidified oil tank 11 or enters the acidized oil tank 11 through the oil phase circulation unit, and the other...

Embodiment 3

[0056]A kind of technique of continuously producing acidified oil and by-product sodium sulfate crystal by soybean soapstock raw material, it utilizes the device of embodiment 1, and concrete process flow step is as follows: add 35% sulfuric acid aqueous solution in the reactor 4, the soybean in the raw material tank 13 The soapstock raw material, after being heated to 50° C., passes through the raw material pump, and enters the reactor 4 after being heated to 70° C. by the heater 9 at a processing rate of 2 tons per hour. The acidification reaction takes place in reactor 4 . The upper oil layer enters the settling tank 5 through the outlet at the upper end of the reactor. The fatty acid in the upper layer of the settling tank 5 overflows to the circulating oil tank 7, and the part of the acidified oil in the circulating oil tank 7 forms a mixed oil product with the raw material through the heater 9 and returns to the reactor 4 to establish oil circulation, and the mixed solut...

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Abstract

The invention provides a device for continuously producing an acidified oil and co-producing a sodium sulfate crystal from nigre. The device comprises a suction filtration tank, a reactor, a settlingtank, a buffer tank, a circulating oil tank, an acid liquid circulating pump, a heater, a circulating oil pump, an acidified oil tank, a raw material pump, a raw material tank, an acid preparation tank and an acid discharge pump, wherein the reactor is provided with an acid liquid feed port, a nigre feed port, an upper discharge port and a lower discharge port; the raw material tank is connected to the heater through the raw material pump; the heater is connected with the nigre feed port of the reactor; the upper discharge port of the reactor is connected to the settling tank; the lower discharge port is connected to the suction filtration tank; the self-priming buffer tank is connected with the bottom of the settling tank through a self-priming pipe and is connected to the acid liquid feed port of the reactor through the acid liquid circulating pump; the settling tank is provided with an overflow port connected to the circulating oil tank; the circulating oil tank is connected to thecirculating oil pump; the circulating oil pump is respectively connected to the heater and the acidified oil tank; the acid preparation tank and the suction filtration tank are connected to the acid discharge pump; and the acid discharge pump is connected to the acid liquid feed port of the reactor.

Description

technical field [0001] The invention generally belongs to the technical field of soapstock processing, and in particular relates to a device for producing acidified oil and by-product sodium acid crystals from soapstock. Background technique [0002] Acidified oil refers to the oil obtained by acidifying the by-product soapstock produced in oil refineries. Main use: used in cold drawing factories, steel factories, and also used in pharmaceutical factories, medical care, feed factories, brick and tile factories for demoulding (isolation). Acidified oils can be used to produce fatty acids, oleic acid, stearic acid, fatty acid methyl esters, plasticizers. [0003] The current production method of acidified oil is mainly obtained by acidifying soapstock. Soapstock is a by-product of the oil refining process, which contains neutral oil (8-27%), soap (sodium fatty acid) 30-40%, the rest is mainly water, and a small amount of free fatty acids, phospholipids and lipids And pigmen...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C11B13/02C01D5/00
CPCY02W30/74
Inventor 靳辉唐强姜顺波杨金雁刘莹
Owner 山东格瑞材料科技有限公司
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