CN207446200U - A kind of hydrogenation reaction kettle for WHITE OIL PRODUCTION line - Google Patents
A kind of hydrogenation reaction kettle for WHITE OIL PRODUCTION line Download PDFInfo
- Publication number
- CN207446200U CN207446200U CN201720956757.7U CN201720956757U CN207446200U CN 207446200 U CN207446200 U CN 207446200U CN 201720956757 U CN201720956757 U CN 201720956757U CN 207446200 U CN207446200 U CN 207446200U
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- China
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- catalyst
- tank body
- group
- production line
- tail oil
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Abstract
A kind of hydrogenation reaction kettle for WHITE OIL PRODUCTION line, it includes tank body（1）, catalyst babinet（2）, catalyst flow valve（3）, integrated package（10）, one group of equal stringing of catalyst（4）, force (forcing) pump（5）, pressure-control valve（6）, tail oil pipe（7）, outlet valve（8）And hydrogen pipe（12）, the tank body（1）Top surface be equipped with one group of catalyst inlet, bottom is taper, and bottom is equipped with discharge port, and side surface upper part is equipped with tail oil entrance and hydrogenation mouth;Advantage is：It is reasonable in design, it is precisely controlled the additive amount of catalyst automatically using flow valve, simultaneously catalyst is added in a manner that top is uniformly distributed, catalyst is made fully to be contacted with tail oil and hydrogen, accelerate tail oil reaction fission process, make reaction more thorough, improve WHITE OIL PRODUCTION line efficiency, reduce cost, there is good practical value.
Description
Technical field
The utility model is related to WHITE OIL PRODUCTION technical fields, and in particular to a kind of hydrogenation reaction for WHITE OIL PRODUCTION line
Kettle.
Background technology
Shortening shortening, scientific name white oil because it seems snow-white, are similar to lard.Shortening is food industry
One of special fat.It has certain plasticity or denseness, the purposes such as dispensing, surface spraying or the demoulding as cake.It
Can be used to shortcakeization or soften baked food, make protein and carbohydrate in process will not become it is hard and
It is linked to be bulk, and improves mouthfeel.
At present, the production for eating white oil is generally produced using one-stage hydrogenation technique, and one-stage hydrogenation technique is to be hydrocracked
It is raw material that tail oil or SSOT tail oils, which pass through solvent dewaxed oil, using reduced form metallic catalyst by being hydrogenated under elevated pressure conditions,
Product directly passes through the opening of retort in existing production line after the usual manual weighing of addition of catalyst at present up to food-grade
Directly plus people, this plus catalyst mode are unfavorable for contact of the catalyst with tail oil and hydrogen, and are unfavorable for integral sealing and set
Meter, can drag long response time process, slow down production line beat, increase production cost.
Utility model content
The purpose of this utility model be exactly in order to solve the above-mentioned technical problem, and provide it is a kind of for WHITE OIL PRODUCTION line plus
Hydrogen reaction kettle.
The utility model include tank body, catalyst babinet, catalyst flow valve, integrated package, the equal stringing of one group of catalyst, plus
Press pump, pressure-control valve, tail oil pipe, outlet valve and hydrogen pipe, the top surface of the tank body are equipped with one group of catalyst inlet, bottom
For taper, bottom is equipped with discharge port, and side surface upper part is equipped with tail oil entrance and hydrogenation mouth, and side lower is equipped with pressurization mouth, in side
Portion is equipped with visual window installing port, and the catalyst babinet is fixed by the bracket mounted on the top of tank body, and the integrated package is equipped with
Entrance, one group of outlet and the inner passage for connecting inlet port, the entrance of integrated package pass through catalyst flow valve and catalyst tank
The outlet of body, one group of outlet with integrated package, the other end are distinguished respectively for one end of the equal stringing of one group of catalyst
It being connected with tank body top surface equipped with one group of catalyst inlet, the housing of the force (forcing) pump is fixedly mounted on the outer wall of tank body, and
The high-pressure outlet of force (forcing) pump is connected by pressure-control valve and pipeline with the pressurization mouth of tank body, the tail oil of the tail oil pipe and tank body
Entrance connects, and the outlet valve is mounted on the discharge outlet of tank body, and the hydrogen pipe is connected by valve with the hydrogenation mouth of tank body.
It also has glass vision panel, and the glass vision panel is fixedly mounted at the visual window installing port of tank body.
The top of the tank body is plane, and bottom is taper.
The utility model advantage is：The utility model provides a kind of hydrogenation reaction kettle for WHITE OIL PRODUCTION line, and structure is set
Meter is reasonable, is precisely controlled the additive amount of catalyst automatically using flow valve, while adds in catalyst in a manner that top is uniformly distributed,
Catalyst is made fully to be contacted with tail oil and hydrogen, accelerates tail oil reaction fission process, makes reaction more thorough, improve WHITE OIL PRODUCTION
Line efficiency reduces cost, has good practical value.
Description of the drawings
Fig. 1 is the utility model structure diagram.
Specific embodiment
As shown in drawings, the utility model includes tank body 1, catalyst babinet 2, catalyst flow valve 3, integrated package 10, one
The equal stringing 4 of group catalyst, force (forcing) pump 5, pressure-control valve 6, tail oil pipe 7, outlet valve 8 and hydrogen pipe 12, the top surface of the tank body 1
One group of catalyst inlet is equipped with, bottom is taper, and bottom is equipped with discharge port, and side surface upper part is equipped with tail oil entrance and hydrogenation mouth,
Side lower is equipped with pressurization mouth, is equipped with visual window installing port in the middle part of side, the catalyst babinet 2 is fixedly mounted by stent 9
At the top of tank body 1, the integrated package 10 is equipped with entrance, one group of outlet and the inner passage for connecting inlet port, integrated package 10
Entrance pass through the outlet of catalyst flow valve 3 and catalyst babinet 2, one end point of the equal stringing 4 of one group of catalyst
Not with one group of outlet of integrated package 10, the other end connects respectively with 1 top surface of tank body equipped with one group of catalyst inlet, described
The housing of force (forcing) pump 5 is fixedly mounted on the outer wall of tank body 1, and the high-pressure outlet of force (forcing) pump 5 passes through pressure-control valve 6 and pipeline
It is connected with the pressurization mouth of tank body 1, the tail oil pipe 7 is connected with the tail oil entrance of tank body 1, and the outlet valve 8 is mounted on tank body 1
Discharge outlet, the hydrogen pipe 12 are connected by valve with the hydrogenation mouth of tank body 1.
It also has glass vision panel 11, and the glass vision panel 11 is fixedly mounted at the visual window installing port of tank body 1.
The top of the tank body 1 is plane, and bottom is taper.
Working method and principle：In use, adding in tail oil to be reacted from tail oil pipe 7, hydrogen pipe 12 passes through technically pure
Hydrogen, catalyst are added in catalyst babinet 2, and according to tail oil inlet, force (forcing) pump 5 opens work to adding in tank body 1
Pressure, pressure-control valve 6 control 1 internal pressure of tank body to try hard to keep and hold setting pressure, and catalyst flow valve 3 controls catalyst needed for primary first-order equation
Amount, and from equal 4 even drop down of stringing of one group of catalyst in a manner that top uniformly falls, make catalyst fully with tail oil and hydrogen
Gas contacts, and accelerates tail oil reaction fission process, makes reaction more thorough, improve WHITE OIL PRODUCTION line efficiency, reduce cost.
Claims (3)
1. a kind of hydrogenation reaction kettle for WHITE OIL PRODUCTION line, it is characterised in that it includes tank body（1）, catalyst babinet（2）, urge
Agent flow valve（3）, integrated package（10）, one group of equal stringing of catalyst（4）, force (forcing) pump（5）, pressure-control valve（6）, tail oil pipe
（7）, outlet valve（8）And hydrogen pipe（12）, the tank body（1）Top surface be equipped with one group of catalyst inlet, bottom is taper, bottom
Portion is equipped with discharge port, and side surface upper part is equipped with tail oil entrance and hydrogenation mouth, and side lower is equipped with pressurization mouth, is equipped in the middle part of side visual
Window installing port, the catalyst babinet（2）Pass through stent（9）It is fixedly mounted on tank body（1）Top, the integrated package（10）If
There are entrance, one group of outlet and the inner passage for connecting inlet port, integrated package（10）Entrance pass through catalyst flow valve（3）With
Catalyst babinet（2）Outlet, the equal stringing of one group of catalyst（4）One end respectively with integrated package（10）One group go out
Mouthful connection, the other end respectively with tank body（1）Top surface is equipped with one group of catalyst inlet and connects, the force (forcing) pump（5）Housing consolidate
Dingan County is mounted in tank body（1）Outer wall on, and force (forcing) pump（5）High-pressure outlet pass through pressure-control valve（6）With pipeline and tank body（1）
Pressurization mouth connection, the tail oil pipe（7）With tank body（1）Tail oil entrance connection, the outlet valve（8）Mounted on tank body（1）
Discharge outlet, the hydrogen pipe（12）Pass through valve and tank body（1）Hydrogenation mouth connection.
2. a kind of hydrogenation reaction kettle for WHITE OIL PRODUCTION line according to claim 1, it is characterised in that it also has glass
Form（11）, the glass vision panel（11）It is fixedly mounted on tank body（1）Visual window installing port at.
A kind of 3. hydrogenation reaction kettle for WHITE OIL PRODUCTION line according to claim 1, it is characterised in that the tank body（1）
Top for plane, bottom is taper.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720956757.7U CN207446200U (en) | 2017-08-02 | 2017-08-02 | A kind of hydrogenation reaction kettle for WHITE OIL PRODUCTION line |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720956757.7U CN207446200U (en) | 2017-08-02 | 2017-08-02 | A kind of hydrogenation reaction kettle for WHITE OIL PRODUCTION line |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207446200U true CN207446200U (en) | 2018-06-05 |
Family
ID=62248929
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720956757.7U Expired - Fee Related CN207446200U (en) | 2017-08-02 | 2017-08-02 | A kind of hydrogenation reaction kettle for WHITE OIL PRODUCTION line |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207446200U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2021159790A1 (en) * | 2020-02-13 | 2021-08-19 | 东营联合石化有限责任公司 | Petroleum hydrocracking reaction apparatus |
-
2017
- 2017-08-02 CN CN201720956757.7U patent/CN207446200U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2021159790A1 (en) * | 2020-02-13 | 2021-08-19 | 东营联合石化有限责任公司 | Petroleum hydrocracking reaction apparatus |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180605 Termination date: 20200802 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |