Wet type polyurethane joint material for thermal insulation for seabed oil and gas pipeline interface and preparation method of wet type polyurethane joint material
A technology of oil and gas pipelines and polyurethane, which is applied in the field of polyurethane node materials and its preparation, which can solve the problems of less than 100% closed cell rate, high water absorption rate of materials, and low compressive strength, and achieve low water absorption rate and low mold temperature , the effect of long flow period
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[0036] The following examples are used to further illustrate the preparation and application details of the present invention, and do not constitute a limitation on the spirit and scope of the present invention.
[0037] The experimental methods used in the following examples are conventional methods unless otherwise specified.
[0038] The materials and reagents used in the following examples can be obtained from commercial sources unless otherwise specified.
[0039] The raw materials used in the following examples are as follows:
[0040] Hydroxyl-terminated polysiloxane DS-3, with a hydroxyl value of 40-50mgKOH / g, from Rhodia, France;
[0041] Polypropylene glycol (PPG-1), hydroxyl value 50~60mgKOH / g, Shandong Bluestar Dongda Company;
[0042] Polyether polyol GE-2, hydroxyl value 160~175mgKOH / g, Shanghai Gaoqiao Petrochemical;
[0043] 1,4-Butanediol (BDO), Diethylene Glycol (DEG), Shanghai Lingfeng Chemical Co., Ltd.;
[0044] Catalyst CT-2X, Aladdin reagent company;
[0045] NCO-B, m...
Embodiment 1
[0052] In a reactor equipped with a vacuum and heating device, mix DS-3 (52.5 parts), PPG-1 (192.5 parts) and GE-2 (105 parts) uniformly and vacuum dry at 95°C for 2.5 hours, then cool slowly After cooling to 60°C, add the dried BDO (85.17 parts) and the catalyst CT-2X (2.85 parts), mix and stir for 15 minutes, then vacuum degas to obtain component A.
[0053] Control the temperature of component A to 30°C, add 564.83 parts of NCO-B, quickly stir and evenly degas, and pour it into a mold with a mold temperature of 70°C to obtain the non-foamed polyurethane node for the submarine pipeline field interface of the present invention material.
[0054] The gel time of the non-foamed polyurethane node material prepared in this embodiment is 5 minutes, and the demolding time is 18 minutes.
[0055] After testing, the initial tensile strength of the node material prepared in this example when demolding is 3.22MPa, the hardness (Shore A) is 70, the tensile strength after post-curing is 18.22M...
Embodiment 2
[0057] In a reactor equipped with a vacuum and heating device, mix DS-3 (17.5 parts), PPG-1 (210.0 parts), and GE-2 (122.5 parts) uniformly and vacuum dry at 95°C for 2.5 hours, then cool slowly After cooling to 50°C, add the dried BDO (83.70 parts) and the catalyst CT-2X (2.85 parts), mix and stir for 15 minutes, then vacuum degas to obtain component A.
[0058] Control the temperature of component A to 30°C, add 566.30 parts of NCO-B, quickly stir and evenly degas, and pour into a mold with a mold temperature of 70°C to obtain the non-foamed polyurethane node for submarine pipeline field interface of the present invention material.
[0059] The gel time of the non-foamed polyurethane node material prepared in this embodiment is 4 minutes, and the demolding time is 16 minutes.
[0060] After testing, the initial strength of the node material prepared in this example when demolding is 4.13 MPa, the hardness (Shore A) is 78, the tensile strength after post-curing is 14.46 MPa, the el...
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