Device and process for producing undecylenic acid methyl ester using methyl ricinoleate as raw material
US-10081590-B2 · Sep 25, 2018 · US
US11407948B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11407948-B2 |
| Application number | US-201817047707-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 28, 2018 |
| Priority date | Jan 30, 2018 |
| Publication date | Aug 9, 2022 |
| Grant date | Aug 9, 2022 |
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A device for pyrolysis reactions includes a feeding pump, a flow meter, an atomizer, a pyrolysis reactor, electromagnetic coils, an electromagnetic induction heating power, a temperature sensor, a temperature controller, a condenser and a product tank. The feeding pump is connected with the flow meter which is connected to the inlet of the atomizer in the pyrolysis reactor. There is a port at the bottom of the pyrolysis reactor, with the port at the top of the pyrolysis reactor connected with the condenser. The condenser is connected with the product tank. The external wall of the pyrolysis reactor is surrounded by electromagnetic coils which are connected with the electromagnetic induction heating power. The temperature sensor is placed between the pyrolysis reactor and the coils, which is connected with the temperature controller. The contact resistance between the atomized material and the hot surface can be.
Opening claim text (preview).
What is claimed is: 1. A device for pyrolysis reactions comprising: a feeding pump, a flow meter, an atomizer having an inlet, a pyrolysis reactor having a port at a bottom and a ort at a top, electromagnetic coils, an electromagnetic induction heating power, a temperature sensor, a temperature controller, a condenser and a product tank, wherein the feeding pump is connected with the flow meter which is connected to the inlet of the atomizer in the pyrolysis reactor wherein the port at the top of the pyrolysis reactor is connected with the condenser, wherein the condenser is connected with the product tank, wherein the external wall of the pyrolysis reactor is surrounded by the electromagnetic coils which are connected with the electromagnetic induction heating power, wherein the temperature sensor is placed between the pyrolysis reactor and the electromagnetic coils, wherein the temperature sensor is connected with the temperature controller, and wherein the atomizer is centrally positioned inside the pyrolysis reactor. 2. The device for pyrolysis reactions according to claim 1 , wherein pyrolysis reactor is made of a material selected from one of stainless iron, carbon steel, iron and high temperature resistant and magnetically permeable materials. 3. The device for pyrolysis reactions according to claim 1 , wherein the atomizer is one of a nozzle type atomizer and a centrifugal type atomizer, wherein the nozzle type atomizer includes one of single nozzle, multiple nozzles at single layer, and multiple nozzles at multiple layers, wherein a nozzle of the nozzle type atomizer is mounted to a vertical feeding pipe having an axis, wherein said nozzle is one of fixedly mounted to the feeding pipe and rotatable mounted to the feeding pipe, wherein the atomizer is made of a material selected from one of stainless steel, copper and high temperature resistant materials with low magnetic permeability. 4. The device for pyrolysis reactions according to claim 1 , the temperature sensor is configured as one of a thermocouple and a thermistor, wherein the temperature sensor is arranged to have a temperature measurement point at a center of the electromagnetic coils. 5. The device for pyrolysis reactions according to claim 1 , wherein the feeding pump is configured to introduce at least one of liquid feedstock and slurry fluid feedstock. 6. The device for pyrolysis reactions according to claim 1 , wherein the condenser includes four ports and the product tank includes three ports, wherein a first port of the condenser is connected with the port at the top of the pyrolysis reactor, and wherein a second port of the condenser is connected with an input port of the product tank.
Nozzle-type elements (nozzle-type reactors B01J19/26) · CPC title
Pyrolysis reactions (of hydrocarbons C10G9/00) · CPC title
Heat treatments such as} Calcining; Fusing {; Pyrolysis (furnaces F27D) · CPC title
Apparatus · CPC title
Stationary reactors without moving elements inside (B01J19/08, B01J19/26 take precedence; with stationary particles B01J8/02) · CPC title
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