Process and device for continuous acidification of acidification section in production of sebacic acid

A sebacic acid and process technology, applied in the field of continuous acidification process and its process equipment, can solve problems such as restricting the development of enterprises and industries, waste of water resources, energy, and inability to achieve continuous production, and achieve quality assurance, stable operation, and overcoming problems. The effect of corrosion and acidification crystallizing tank

Inactive Publication Date: 2014-09-24
SHANDONG TIANXING BIOTECH
View PDF3 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the acidification process in sebacic acid production in China generally adopts the intermittent acidification process. In the acidification process, the acidification heating reaction, crystallization and thickening are all carried out in the same reaction tank. From feeding to discharging, They are all produced in tanks, which cannot achieve continuous flow-through production, which seriously restricts the output. The automation level of equipment and devices is low, and the technology is backward, resulting in low production efficiency and unstable product quality.
In addition, when the temperature is lowered slowly in intermittent acidification, the primary water valve is opened too large, and the coil is easy to accumulate material, which reduces the cooling effect and prolongs the cooling time. In order to shorten the cooling time, a large amount of circulating water must be supplied, resulting in serious waste of water resources and energy. High production costs and many other issues
At present, the backward technology has seriously restricted the development of enterprises and industries

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Process and device for continuous acidification of acidification section in production of sebacic acid
  • Process and device for continuous acidification of acidification section in production of sebacic acid
  • Process and device for continuous acidification of acidification section in production of sebacic acid

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] According to the sebacic acid production continuous acidification process of the present invention, comprises the following steps:

[0028]The decolorizing liquid is heated to 92°C with steam in the storage tank, pumped into the acidifier through a rotameter with a pipeline pump, and at the same time, sulfuric acid is added to the acidifier at a ratio of 15% to control the pH value of the feed liquid at 2. The liquid flows from the acidifier to the first heating tank by virtue of the high level difference, and the heater is used in the first heating tank to heat the feed liquid to above 100°C, so that the feed liquid is mixed and boiled, and the feed liquid flows to the second heating tank by itself. Continue heating to further make the feed liquid fully boil. The feed liquid flows from the second heating tank to the acidification crystallization tank. 27 revolutions per minute, after the feed liquid passes through the fourth to seventh stage acidification crystallizati...

Embodiment 2

[0030] According to the sebacic acid production continuous acidification process of the present invention, comprises the following steps:

[0031] The decolorizing liquid is heated to 96°C with steam in the storage tank, pumped into the acidifier through a rotameter with a pipeline pump, and at the same time, sulfuric acid is added to the acidifier at a ratio of 18%, and the pH value of the feed liquid is controlled at 1.5. The liquid flows from the acidifier to the first heating tank by virtue of the high level difference, and the heater is used in the first heating tank to heat the feed liquid to above 100°C, so that the feed liquid is mixed and boiled, and the feed liquid flows to the second heating tank by itself. Continue heating to further make the feed liquid fully boil. The feed liquid flows from the second heating tank to the acidification crystallization tank. 30 revolutions per minute, after the feed liquid passes through the fourth to seventh stage acidification cr...

Embodiment 3

[0033] According to the sebacic acid production continuous acidification process of the present invention, comprises the following steps:

[0034] The decolorization liquid is heated to 97°C with steam in the storage tank, and then pumped into the acidifier through a rotameter with a pipeline pump. At the same time, 20% sulfuric acid is added to the acidifier to control the pH value of the feed liquid at 1.5. The liquid flows from the acidifier to the first heating tank by virtue of the high level difference, and the heater is used in the first heating tank to heat the feed liquid to above 100°C, so that the feed liquid is mixed and boiled, and the feed liquid flows to the second heating tank by itself. Continue heating to further make the feed liquid fully boil. The feed liquid flows from the second heating tank to the acidification crystallization tank. 25 revolutions per minute, after the feed liquid passes through the acidification crystallization tank from the fourth to t...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The invention relates to the technical field of production of sebacic acid and discloses a process and a device for continuous acidification of an acidification section in production of sebacic acid. The process comprises the following steps of: heating a decoloring solution obtained in advance of the acidification section in a storage tank, pumping feed liquid into an acidifier for the acidification by a pipeline pump through a rotor flow meter, heating the feed liquid in a heating tank, cooling and crystallizing the feed liquid in an acidification crystallizing tank, and carrying out layering in a thickener through gravity settling; and after the layering in the thickener through the gravity settling is carried out, filtering clear mother liquid at the upper layer through a filter, discharging filtrate to a wastewater pool, and separating thick sebacic acid liquid (which flows to a drying procedure independently) at the a lower layer, wherein the continuous and layer-by-layer self-flowing of the feed liquid among the procedures is realized by virtue of the height difference of the feed liquid after the feed liquid is subjected to the acidification through the acidifier and the settlement through the thickener. The process and the device can be used for realizing the continuous production, improving the production efficiency, reducing the production cost, improving the product yield and quality, making the most of secondary water, and saving water resources.

Description

technical field [0001] The invention relates to the field of production of chemical product sebacic acid, in particular to a continuous acidification process and process equipment of the acidification process in the production of sebacic acid. Background technique [0002] Sebacic acid is an important fine chemical intermediate. At present, it is mainly produced from castor oil in the industry. It is also one of the agricultural and forestry chemical products. It has high technological content and high added value. It is widely used in the production of engineering plastics (such as Nylon 1010, Nylon 610, Nylon 810, Nylon 9, Nylon 910, etc.), cold-resistant plasticizers, solvents, softeners, additives, dimethyl sebacate, diethyl sebacate, dioctyl sebacate, Dibutyl sebacate, diisopropyl sebacate, polyester derivatives, etc. In addition, it is also used as a raw material for high temperature resistant lubricating oil, epoxy resin curing agent, sebacic anhydride, synthetic lub...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Patents(China)
IPC IPC(8): C07C55/20C07C51/02
Inventor 怀进步
Owner SHANDONG TIANXING BIOTECH
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products