Some calculations are made for the utilization of waste heat in the tail gas from preneutralization,pipe reaction and secondary ammoniation sections.

介绍应的尾气与管式应及二次氨化应尾气混合洗涤后的尾气余热利用的有关计算。

An analysis is made of the present status of production of DAP by the mixed process of preneutralization reactor tank-pipe reactor,as the moisture content of the product fluctuates greatly.

针应槽-管式应器混合工艺生产磷酸二铵产品时,产品水含量波动较大的生产现状进行了分析。

Some calculations are made for the utilization of waste heat in the tail gas from preneutralization,pipe reaction and secondary ammoniation sections.

介绍预反应的尾气与管式反应及二次氨化反应尾气混合洗涤后的尾气余热利用的有关计算。

An analysis is made of the present status of production of DAP by the mixed process of preneutralization reactor tank-pipe reactor,as the moisture content of the product fluctuates greatly.

针对预反应槽-管式反应器混合工艺生产磷酸二铵产品时,产品水含量波动较大的生产现状进行了析。

Some calculations are made for the utilization of waste heat in the tail gas from preneutralization,pipe reaction and secondary ammoniation sections.

介绍预和反应的尾气与管式反应及二次氨化反应尾气混合洗涤后的尾气余热利用的有关计算。

An analysis is made of the present status of production of DAP by the mixed process of preneutralization reactor tank-pipe reactor,as the moisture content of the product fluctuates greatly.

针对预和反应槽-管式反应器混合工艺生产磷酸二铵产品时,产品水含量波动较大的生产现状进行了分析。

Some calculations are made for the utilization of waste heat in the tail gas from preneutralization,pipe reaction and secondary ammoniation sections.

介绍预和反应的与管式反应及二次氨化反应合洗涤后的余热利用的有关计算。

An analysis is made of the present status of production of DAP by the mixed process of preneutralization reactor tank-pipe reactor,as the moisture content of the product fluctuates greatly.

针对预和反应槽-管式反应器合工艺生磷酸二铵,水含量波动较大的生现状进行了分析。

Some calculations are made for the utilization of waste heat in the tail gas from preneutralization,pipe reaction and secondary ammoniation sections.

介绍预和的气与管式及二次氨化气混合洗涤后的气余热利用的有关计算。

An analysis is made of the present status of production of DAP by the mixed process of preneutralization reactor tank-pipe reactor,as the moisture content of the product fluctuates greatly.

针对预和槽-管式器混合工艺生磷酸二铵,水含量波动较大的生现状进行了分析。

Some calculations are made for the utilization of waste heat in the tail gas from preneutralization,pipe reaction and secondary ammoniation sections.

介绍预和的气与管式及二次氨化气混合洗涤后的气余热利用的有关计算。

An analysis is made of the present status of production of DAP by the mixed process of preneutralization reactor tank-pipe reactor,as the moisture content of the product fluctuates greatly.

针对预和槽-管式器混合工艺生磷酸二铵,水含量波动较大的生现状进行了分析。

Some calculations are made for the utilization of waste heat in the tail gas from preneutralization,pipe reaction and secondary ammoniation sections.

介绍预和反应的尾气与管式反应及二次氨化反应尾气混合洗涤后的尾气余热利用的有关计算。

An analysis is made of the present status of production of DAP by the mixed process of preneutralization reactor tank-pipe reactor,as the moisture content of the product fluctuates greatly.

针对预和反应槽-管式反应器混合工艺生产磷酸二铵产品时,产品水含量波动较大的生产现状进行了分析。

Some calculations are made for the utilization of waste heat in the tail gas from preneutralization,pipe reaction and secondary ammoniation sections.

介绍预和反应尾气反应及二次氨化反应尾气混合洗涤后尾气余热利用有关计算。

An analysis is made of the present status of production of DAP by the mixed process of preneutralization reactor tank-pipe reactor,as the moisture content of the product fluctuates greatly.

针对预和反应槽-反应器混合工艺磷酸二铵品时,品水含量波动较大现状进行了分析。

Some calculations are made for the utilization of waste heat in the tail gas from preneutralization,pipe reaction and secondary ammoniation sections.

介绍预和反尾气与管式反及二次氨化反尾气合洗涤后尾气余热有关计算。

An analysis is made of the present status of production of DAP by the mixed process of preneutralization reactor tank-pipe reactor,as the moisture content of the product fluctuates greatly.

针对预和反槽-管式反合工艺生产磷酸二铵产品时,产品水含量波动较大生产现状进行了分析。