CN109486528A - A kind of device producing Fischer-Tropsch wax crude product - Google Patents

A kind of device producing Fischer-Tropsch wax crude product Download PDF

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Publication number
CN109486528A
CN109486528A CN201811645575.3A CN201811645575A CN109486528A CN 109486528 A CN109486528 A CN 109486528A CN 201811645575 A CN201811645575 A CN 201811645575A CN 109486528 A CN109486528 A CN 109486528A
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CN
China
Prior art keywords
fischer
entrance
tropsch wax
connect
outlet
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201811645575.3A
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Chinese (zh)
Inventor
刘新涛
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dalian Lonsin New Materials Co Ltd
Original Assignee
Dalian Lonsin New Materials Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Dalian Lonsin New Materials Co Ltd filed Critical Dalian Lonsin New Materials Co Ltd
Priority to CN201811645575.3A priority Critical patent/CN109486528A/en
Publication of CN109486528A publication Critical patent/CN109486528A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G73/00Recovery or refining of mineral waxes, e.g. montan wax
    • C10G73/02Recovery of petroleum waxes from hydrocarbon oils; Dewaxing of hydrocarbon oils
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G73/00Recovery or refining of mineral waxes, e.g. montan wax
    • C10G73/02Recovery of petroleum waxes from hydrocarbon oils; Dewaxing of hydrocarbon oils
    • C10G73/025Recovery of petroleum waxes from hydrocarbon oils; Dewaxing of hydrocarbon oils by filtration

Abstract

The present invention relates to a kind of devices for producing Fischer-Tropsch wax crude product, belong to Fischer-Tropsch wax production technical field.Device of the present invention includes reaction kettle, filter, preheater, thin film evaporator;The outlet of the reaction kettle and the entrance of filter connect;The outlet of the filter and the entrance of preheater connect;The outlet of the preheater and the entrance of thin film evaporator connect.Fischer-Tropsch wax is slightly purified by carclazyte decoloring reaction, filtering, thin film evaporation using device of the present invention, there are simple operation and other advantages.

Description

A kind of device producing Fischer-Tropsch wax crude product
Technical field
The present invention relates to a kind of devices for producing Fischer-Tropsch wax crude product, belong to Fischer-Tropsch wax production technical field.
Background technique
Fischer-Tropsch wax is the wax that coal gas is produced by F- T synthesis, and main component is C12-C90 alkane, normal paraffin content Up to 80% or more, fusing point is up to 90 DEG C or more.It is made of relative molecular mass in the straight chain of 200-1200, the High-carbon alkane of saturation, With fine crystal structure, high-melting-point, low oil content, low needle penetration, low mobility, low melting viscosity, hard, wear-resisting and steady The advantages that qualitative high.
Fischer-Tropsch wax is mainly used for hot melt adhesive, ink and coating, plastic processing (PVC lubricant, polyene hydrocarbon lubricants and color masterbatch Pellet dispersing agent) etc. fields.
Fischer-Tropsch wax is ideal synthetic wax used in EVA based melt adhesive, and dystectic wax can be improved the heat-resisting of adhesive Property and quick-drying.
When Fischer-Tropsch wax with particle sprills use in ink, wearability, the wrinkle resistance of application material can be improved, apply In coating, corrugation effect can be played, striped and water wave corrugation effect can be formed in micronised state use, powder is being added Coating resin plays lubricating action in extrusion process, can reduce screw torque, reduces energy consumption and improves production efficiency.
Fischer-Tropsch wax is obvious with stabilizer synergy with PVC processing, can effectively extend heat-stable time, increases process warm The amplitude of accommodation of degree, it is particularly evident in the processing of CPVC resin, since CPVC resin processing techniques parameter regulation narrow range increases The difficulty of processing of product can be effectively improved the later period lubrication of CPVC product processing, promote the appearance and mechanical property of product.
Summary of the invention
The present invention, to black wax decoloration, filtering, thin film evaporation containing Fischer-Tropsch wax and catalyst, obtains Fischer-Tropsch using new equipment Wax crude product is using the raw material or other purposes as high-quality Fischer-Tropsch wax product.
The present invention provides a kind of device for producing Fischer-Tropsch wax crude product, described device includes reaction kettle, filter, preheating Device, thin film evaporator;The outlet of the reaction kettle and the entrance of filter connect;The outlet of the filter and entering for preheater Mouth connection;The outlet of the preheater and the entrance of thin film evaporator connect.
The present invention is preferably that the filter is plate filter or frame filter.
The present invention is preferably that described device includes storage tank;The outlet of the filter and the entrance of storage tank connect;The storage The outlet of tank and the entrance of preheater connect.
The present invention is preferably that described device includes surge tank I, surge tank II;The water of the thin film evaporator and before distillate mouth It is connect with the entrance of surge tank I;The Fischer-Tropsch wax crude product outlet of the thin film evaporator is connect with the entrance of surge tank II.
The invention has the following beneficial effects:
Fischer-Tropsch wax is slightly purified by carclazyte decoloring reaction, filtering, thin film evaporation using device of the present invention, is had There are simple operation and other advantages.
Detailed description of the invention
3 width of attached drawing of the present invention,
Fig. 1 is the structural schematic diagram that Fischer-Tropsch wax crude product device is produced described in embodiment 1;
Fig. 2 is the structural schematic diagram that Fischer-Tropsch wax crude product device is produced described in embodiment 2;
Fig. 3 is the structural schematic diagram that Fischer-Tropsch wax crude product device is produced described in embodiment 3;
Wherein, 1, reaction kettle, 2, filter, 3, preheater, 4, thin film evaporator, 5, storage tank, 6, surge tank I, 7, buffering Tank II.
Specific embodiment
Following non-limiting embodiments can with a person of ordinary skill in the art will more fully understand the present invention, but not with Any mode limits the present invention.
Embodiment 1
A kind of device producing Fischer-Tropsch wax crude product, described device include reaction kettle 1, filter 2, preheater 3, film steaming Send out device 4;
The filter 2 is plate filter 2;
The outlet of the reaction kettle 1 is connect with the entrance of plate filter 2;
The outlet of the plate filter 2 is connect with the entrance of preheater 3;
The outlet of the preheater 3 is connect with the entrance of thin film evaporator 4.
Embodiment 2
A kind of device producing Fischer-Tropsch wax crude product, described device include reaction kettle 1, filter 2, storage tank 5, preheater 3, Thin film evaporator 4;
The filter 2 is frame filter 2;
The outlet of the reaction kettle 1 is connect with the entrance of frame filter 2;
The outlet of the frame filter 2 is connect with the entrance of storage tank 5;
The outlet of the storage tank 5 is connect with the entrance of preheater 3;
The outlet of the preheater 3 is connect with the entrance of thin film evaporator 4.
Embodiment 3
A kind of device producing Fischer-Tropsch wax crude product, described device include reaction kettle 1, filter 2, storage tank 5, preheater 3, Thin film evaporator 4, surge tank I 6, surge tank II 7;
The filter 2 is plate filter 2;
The outlet of the reaction kettle 1 is connect with the entrance of plate filter 2;
The outlet of the plate filter 2 is connect with the entrance of storage tank 5;
The outlet of the storage tank 5 is connect with the entrance of preheater 3;
The outlet of the preheater 3 is connect with the entrance of thin film evaporator 4;
The water of the thin film evaporator 4 and before distillate mouth and connect with the entrance of surge tank I 6;
The Fischer-Tropsch wax crude product outlet of the thin film evaporator 4 is connect with the entrance of surge tank II 7.
Application examples 1
A method of Fischer-Tropsch wax crude product being prepared using 3 described device of embodiment, the preparation method includes following step It is rapid:
1. black wax is added in reaction kettle 1, melted at 130 DEG C, the carclazyte stirring for adding black wax weight 8% is de- Color is filtered using plate filter 2, obtains the Fischer-Tropsch wax that fusing point is 90-105 DEG C;
2. step Fischer-Tropsch wax 110 DEG C of fusings in storage tank 5 that 1. gained fusing point is 90-105 DEG C are obtained liquid Fischer-Tropsch Wax;
3. 2. step is added in thin film evaporator 4 after gained liquid Fischer-Tropsch wax improves temperature by preheater 3, film The condition of evaporation are as follows: temperature is 180 DEG C, vacuum degree 50Pa, knifing rotating speed 120rpm, and condensation temperature is 70 DEG C, Leng Jingwen Degree is 20 DEG C, and the water sloughed and before evaporating is temporarily stored in surge tank I 6, obtains Fischer-Tropsch wax crude product and is temporarily stored in surge tank II 7.

Claims (4)

1. a kind of device for producing Fischer-Tropsch wax crude product, it is characterised in that: described device include reaction kettle, filter, preheater, Thin film evaporator;
The outlet of the reaction kettle and the entrance of filter connect;
The outlet of the filter and the entrance of preheater connect;
The outlet of the preheater and the entrance of thin film evaporator connect.
2. producing the device of Fischer-Tropsch wax crude product according to claim 1, it is characterised in that: the filter is plate-type filtering Machine or frame filter.
3. producing the device of Fischer-Tropsch wax crude product according to claim 2, it is characterised in that: described device includes storage tank;
The outlet of the filter and the entrance of storage tank connect;
The outlet of the storage tank and the entrance of preheater connect.
4. according to claim 3 produce Fischer-Tropsch wax crude product device, it is characterised in that: described device include surge tank I, Surge tank II;
The water of the thin film evaporator and before distillate mouth and connect with the entrance of surge tank I;
The Fischer-Tropsch wax crude product outlet of the thin film evaporator is connect with the entrance of surge tank II.
CN201811645575.3A 2018-12-29 2018-12-29 A kind of device producing Fischer-Tropsch wax crude product Pending CN109486528A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811645575.3A CN109486528A (en) 2018-12-29 2018-12-29 A kind of device producing Fischer-Tropsch wax crude product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811645575.3A CN109486528A (en) 2018-12-29 2018-12-29 A kind of device producing Fischer-Tropsch wax crude product

Publications (1)

Publication Number Publication Date
CN109486528A true CN109486528A (en) 2019-03-19

Family

ID=65712106

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811645575.3A Pending CN109486528A (en) 2018-12-29 2018-12-29 A kind of device producing Fischer-Tropsch wax crude product

Country Status (1)

Country Link
CN (1) CN109486528A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005121280A1 (en) * 2004-06-08 2005-12-22 Shell Internationale Research Maatschappij B.V. Process to make a base oil
CN101892073A (en) * 2010-07-28 2010-11-24 广州市浩立生物科技有限公司 Method for extracting base oil from cutting line oil
CN205953958U (en) * 2016-07-19 2017-02-15 广州市海珥玛植物油脂有限公司 Oil treatment system of one -level film second grade molecular distillation device
CN207143182U (en) * 2017-05-05 2018-03-27 山西潞安精蜡化学品有限公司 A kind of wax cutting device using three-stage distillation

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005121280A1 (en) * 2004-06-08 2005-12-22 Shell Internationale Research Maatschappij B.V. Process to make a base oil
CN101892073A (en) * 2010-07-28 2010-11-24 广州市浩立生物科技有限公司 Method for extracting base oil from cutting line oil
CN205953958U (en) * 2016-07-19 2017-02-15 广州市海珥玛植物油脂有限公司 Oil treatment system of one -level film second grade molecular distillation device
CN207143182U (en) * 2017-05-05 2018-03-27 山西潞安精蜡化学品有限公司 A kind of wax cutting device using three-stage distillation

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Application publication date: 20190319

RJ01 Rejection of invention patent application after publication