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Multi-stage process for hydrothermal treatment of renewable raw materials

A technology for hydrothermal treatment, raw materials, applied in the direction of biofuels, chemical instruments and methods, fibrous fillers, etc.

Pending Publication Date: 2020-08-18
SUNCOAL INDS
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantage is that, as shown in the example disclosed in DE 10 2008 050 966 A1, lignin derivatives are always used in addition to 40 phr of carbon black or 80 phr of silica / 5 phr of carbon black

Method used

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  • Multi-stage process for hydrothermal treatment of renewable raw materials
  • Multi-stage process for hydrothermal treatment of renewable raw materials
  • Multi-stage process for hydrothermal treatment of renewable raw materials

Examples

Experimental program
Comparison scheme
Effect test

example 12A to example 12D

[0286] For the preparation of rubbers composed of SBR and granular carbon materials from Examples 1 and 2 or with carbon black N660 Examples 12A to 12D of articles and reference examples

[0287] The carbon material obtained according to Example 1 and Example 2 was introduced as filler material into the rubber mixture and vulcanized with the aid of further additives. The components of the rubber mixture are shown in Table 7.

[0288]

[0289] phr: parts per hundred parts of rubber, the amount based on the amount of elastomer

[0290] DPG, CBS: vulcanization accelerator

[0291] Si69: coupling agent

[0292] Table 7

[0293] Lanxess' SBR solution (sSBR) Buna VSL 4526-0 was used as SBR. The SBR is a copolymer composed of 26% by mass of styrene in addition to butadiene. Its Mooney viscosity is 65ME (ASTM D 1646). Zinc oxide, stearic acid and sulfur were from Fischer Scientific. 2-N-Cyclohexylbenzothiazole sulfenamide (CBS) was from Lanxess. 1,3-Diphenylguanidine (D...

example 2

[0301] Application of the particulate carbon material in Example 2 in combination with a coupling agent (Example 12B) caused a noticeable change. Compared to the reference and 12A, the glass transition temperature of the mixture in Example 12 was shifted up to T g,SBR = -0.48°C. Under conditions of weak dynamic strain (0.5%), the energy loss behavior of mixture 12B is clearly improved relative to the reference with N660, which is seen at lower curve changes in the temperature range above the glass transition temperature.

[0302] It can be seen that the elastomeric material comprising the granular carbon material and coupling agent in Example 2 has a smaller value for tan δ above the glass transition temperature relative to the reference with N660, which is shown by the Relatively reduced sliding friction can be expected in the resulting tire.

[0303] tanδ at 60°C tanδ at 0°C Reference with N660 0.1020 1.4342 Example 12A 0.1035 1.4023 Exampl...

example 14

[0312] to confirm 14 C content, the material in Example 2 was provided to A.Mickiewicz University Foundation, Poznań Ridiocarbon Laboratory, ul. 46, 61-612 Poznań. The method used is described by the head of the laboratory, Tomasz Goslar, on the institute's website. The main components of lignin are summarized below.

[0313] Used to use AMS technology to 14 The processing method of C identification age has the following steps:

[0314] a) Chemical pretreatment

[0315] b) Production of CO 2 and graphitized

[0316] c) AMS 14 C measurement

[0317] d) Calculate and calibrate 14 C's age

[0318] a) In principle, chemically pretreated methods are described in Brock et al., 2010, Radiocarbon, 52, 102-112.

[0319] Samples of plant residues were treated with 1M HCl (80°C, 20+min), 0.025M to 0.2M NaOH (80°C), and then, 0.25M HCl (80°C, 1h). After treatment with the corresponding reagents, the samples were rinsed with distilled water (Millipore) until pH=7. If bubble f...

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Abstract

The invention relates to a multi-stage process for the hydrothermal treatment of renewable raw materials, and the method comprises the steps: providing a liquid comprising renewable raw materials, subjecting the liquid to hydrothermal treatment at a temperature between 150 DEG C and 250 DEG C; separating solids from the liquid as much as possible after the hydrothermal treatment, removing the residual humidity of the solids as much as possible by drying, and obtaining a granular carbon material, wherein the STSA surface area and the OAN value are controlled through the concentration of the organic dry amount of the renewable raw material in a liquid containing the renewable raw material, a pH value of the liquid comprising a renewable raw material, an inorganic ion concentration in a liquid comprising the renewable raw material, the temperature of hydrothermal treatment and the retention time in the hydrothermal treatment is controlled by mutual coordination, so the STSA surface area of the minimum 5 m<2> / g and the maximum 200 m<2> / g and the OAN value of the minimum 50 ml / 100 g and the maximum 150 ml / 100 g are adjusted.

Description

[0001] This application is a divisional application of a patent application with the application number 201680068049.8, the application date is November 18, 2016, and the invention title is "a granular carbon material that can be prepared from renewable raw materials and its preparation method". technical field [0002] The invention relates to a granular carbon material, a method for its production and the use of the material in polymer mixtures. Background technique [0003] There are a wide variety of applications for granular carbon materials. One application is as a filler material for polymers such as elastomers, thermoplastics or thermosets. Fillers are used in the production of rubber articles made of elastomers in order to influence the rubber-side properties of the crosslinked rubber article, which are measured, for example, as tensile strength, hardness, rigidity or breaking strength. Furthermore, product properties such as rolling resistance, wear and wet grip i...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B32/05C01B32/15C09K23/00
CPCC09C1/48C09C1/56C08K3/04C08L101/00C08L21/00C01P2006/12C01P2006/19Y02E50/10C09K23/002C08K3/013C08L97/005B60C5/00C08J5/042C01P2004/61C08J2400/26C08J2400/24C08J2400/22C10B53/02B60C1/0016B60C1/0025
Inventor 托比亚斯·维特曼克劳斯·贝格曼
Owner SUNCOAL INDS