我在使用横向模式将一个表格拆分成两个表格时遇到了问题：我尝试从 tablesgeneraton 生成表格以使其正确，但 longtable 命令不起作用，表格在横向模式下从一个页面退出。
服务器没有错误给我任何提示。
我想将其分成两个水平的页面。
这是完整的代码（希望是正确的 MWE - 我无法添加文档类，因为它是定制的，但是article，或者book给我相同的结果）：
\documentclass{book}
\usepackage{pdflscape}
\usepackage{longtable}
\usepackage{booktabs}
\begin{document}
\begin{landscape}
\begin{longtable}{lllllllllll}
\caption{} \\
\label{tab:my-table}\\
\toprule
Reference & Seed generation & Production method & Seed addition & Crystallization unit & Dimensions & Flow pattern & Material and dispersant & Size size control & Yield estimation & Solid loading \\ \midrule
Present work & Off-line & Batch + filtration & Continuous & Tubular microreactor & 1 mm ID, 60 cm L & Two-phase \newline bubble flow & PCM in water & CSD, sieving, \newline filtering & Yes & 2\%, 0.8\% wt \\
\cite{Eder2010} & Off-line & Batch in solution & Continuous & Tubular reactor & 2 mm ID, 15 m L & Single-phase & ASA in ethanol & CSD & 569\% \newline mean mass flow/total seed flow & 5\%wt \\
\cite{Eder2011} & Off-line & Batch in solution & Continuous & Tubular reactor & 2 mm ID, 15 m L & Single-phase & ASA in ethanol & CSD & 779-407-348\% \newline mean mass flow/total seed flow & 7, 14, 16\% wt \\
\cite{Eder2012} & In-line & US-aided nucleation & Continuous & Tubular reactor & 2 mm ID, 27 m L & Two-phase slug flow & ASA in ethanol & CSD & 172-700\% mean mass flow/ \newline total seed flow & Based on relative flow rate \\
\cite{Jiang2014} & In-line & Micromixing (cooling) & Continuous & Tubular reactor & 3.1 mm ID, 15.2 m L & Two-phase slug flow & LAM in water & No & 87\% product solid/total solid & / \\
\cite{Jiang2015} & In-line & US-aided nucleation & Continuous & Tubular reactor & 3.1 mm ID, 15.2 m L & Two-phase slug flow & LAM in water & No & 74\% product solid/ total solid & / \\
\cite{Jordens2017} & In-line & US-aided nucleation and growth & Semi-continuous & Tubular nucleation + \newline batch growth & 5 mm ID, 7 m L tubular nucleation \newline 53x83x97 mm batch vessel & Single-phase & PCM in water & No & No & / \\
\cite{Wong2013} & In-line & Single crystal contact nucleation & Continuous & Nucleator + \newline tubular reactor & 3.2 mm ID \newline 20 ft L & Single-phase & Glycine/PCM in water & CSD & No & Single crystal \\
\cite{MendezDelRio2006} & In-line & Cooling & Continuous & Tubular nucleation (LFTC) + \newline batch growth & 1.6 mm ID, 7.62 m L LFTC \newline 500 ml batch vessel & Single-phase & PCM in ethanol/methanol & No & No & / \\
\cite{Fatemi2021} & In-line & Cooling & Continuous & Tubular microreactor + \newline tubular growth & 1 mm ID, 60 cm L tubular nucleation \newline 2 mm ID, 1.4, 4, 8 m L tubular growth & Two-phase bubble flow & PCM in water & No & 2-70\% measured/ \newline maximum concentration & / \\ \bottomrule
\end{longtable}
\end{landscape}
\end{document}
你能帮我看看我哪里做错了吗？谢谢！
答案1
如果调整列宽，它会适合（但仍然不太易读）：
\documentclass{book}
% not needed as you hav epdflscape\usepackage{lscape}
% not needed here \usepackage{rotating}
% almost never needed in current latex \usepackage{epstopdf}
\usepackage{pdflscape}
\usepackage{longtable}
\usepackage{array,multirow,graphicx}
\usepackage{enumitem}
\usepackage{booktabs}
\begin{document}
\begin{landscape}
\small
\setlength\LTleft{-3cm}
\setlength\tabcolsep{4pt}
\begin{longtable}{@{}
>{\raggedright\arraybackslash}p{1.5cm}
>{\raggedright\arraybackslash}p{2cm}
>{\raggedright\arraybackslash}p{2cm}
>{\raggedright\arraybackslash}p{2cm}
>{\raggedright\arraybackslash}p{2cm}
>{\raggedright\arraybackslash}p{2cm}
>{\raggedright\arraybackslash}p{2cm}
>{\raggedright\arraybackslash}p{2cm}
>{\raggedright\arraybackslash}p{1.5cm}% size and control
>{\raggedright\arraybackslash}p{2cm}
>{\raggedright\arraybackslash}p{1.5cm}% solid loading
@{}}
\caption{} \\
\label{tab:my-table}\\
\toprule
Reference & Seed generation & Production method & Seed addition & Crystall\-iz\-ation unit & Dimensions & Flow pattern & Material and dispersant & Size size control & Yield estimation & Solid loading \\ \midrule
Present work & Off-line & Batch + filtration & Continuous & Tubular microreactor & 1 mm ID, 60 cm L & Two-phase \newline bubble flow & PCM in water & CSD, sieving, \newline filtering & Yes & 2\%, 0.8\% wt \\
\cite{Eder2010} & Off-line & Batch in solution & Continuous & Tubular reactor & 2 mm ID, 15 m L & Single-phase & ASA in ethanol & CSD & 569\% \newline mean mass flow/total seed flow & 5\%wt \\
\cite{Eder2011} & Off-line & Batch in solution & Continuous & Tubular reactor & 2 mm ID, 15 m L & Single-phase & ASA in ethanol & CSD & 779-407-348\% \newline mean mass flow/total seed flow & 7, 14, 16\% wt \\
\cite{Eder2012} & In-line & US-aided nucleation & Continuous & Tubular reactor & 2 mm ID, 27 m L & Two-phase slug flow & ASA in ethanol & CSD & 172-700\% mean mass flow/ \newline total seed flow & Based on relative flow rate \\
\cite{Jiang2014} & In-line & Micromixing (cooling) & Continuous & Tubular reactor & 3.1 mm ID, 15.2 m L & Two-phase slug flow & LAM in water & No & 87\% product solid/total solid & / \\
\cite{Jiang2015} & In-line & US-aided nucleation & Continuous & Tubular reactor & 3.1 mm ID, 15.2 m L & Two-phase slug flow & LAM in water & No & 74\% product solid/ total solid & / \\
\cite{Jordens2017} & In-line & US-aided nucleation and growth & Semi-continuous & Tubular nucleation + \newline batch growth & 5 mm ID, 7 m L tubular nucleation \newline 53x83x97 mm batch vessel & Single-phase & PCM in water & No & No & / \\
\cite{Wong2013} & In-line & Single crystal contact nucleation & Continuous & Nucleator + \newline tubular reactor & 3.2 mm ID \newline 20 ft L & Single-phase & Glycine/PCM in water & CSD & No & Single crystal \\
\cite{MendezDelRio2006} & In-line & Cooling & Continuous & Tubular nucleation (LFTC) + \newline batch growth & 1.6 mm ID, 7.62 m L LFTC \newline 500 ml batch vessel & Single-phase & PCM in ethanol/methanol & No & No & / \\
\cite{Fatemi2021} & In-line & Cooling & Continuous & Tubular microreactor + \newline tubular growth & 1 mm ID, 60 cm L tubular nucleation \newline 2 mm ID, 1.4, 4, 8 m L tubular growth & Two-phase bubble flow & PCM in water & No & 2-70\% measured/ \newline maximum concentration & / \\ \bottomrule
\end{longtable}
\end{landscape}
\end{document}
答案2
基于我之前的建议借助xltabular和threeparttablex，以及较小的字体大小和略微减小的值\tabcolsep，您可以得到以下输出：
\documentclass{book}
\usepackage{pdflscape}
\usepackage{xltabular}
\usepackage{booktabs}
\usepackage{threeparttablex}
\newcolumntype{L}{>{\hspace{0pt}\raggedright\arraybackslash}X}
\begin{document}
\begin{landscape}
\small
\setlength{\tabcolsep}{4pt}
\begin{ThreePartTable}
\begin{TableNotes}
\item[a] mean mass flow/total seed flow
\item[b] product solid/ total solid
\item[c] measured/ maximum concentration
\end{TableNotes}
\begin{xltabular}{\linewidth}{l*{10}{L}}
\caption{}
\label{tab:my-table}\\
\toprule
Reference & Seed generation \& addition & Production method & Crystallization unit & Dimensions & Flow pattern & Material and dispersant & Size size control & Yield estimation & Solid loading \\ \midrule
\endfirsthead
\caption[]{ - continued from previous page}\\
\toprule
Reference & Seed generation \& addition & Production method & Crystallization unit & Dimensions & Flow pattern & Material and dispersant & Size size control & Yield estimation & Solid loading \\ \midrule
\endhead
\bottomrule
\endfoot
\bottomrule
\insertTableNotes
\endlastfoot
Present work & Off-line, Continuous & Batch + filtration & Tubular microreactor & 1 mm ID, 60 cm L & Two-phase bubble flow & PCM in water & CSD, sieving, filtering & Yes & 2\%, 0.8\% wt \\ \addlinespace
\cite{Eder2010} & Off-line, Continuous & Batch in solution & Tubular reactor & 2 mm ID, 15 m L & Single-phase & ASA in ethanol & CSD & 569\%\tnote{a} & 5\%wt \\ \addlinespace
\cite{Eder2011} & Off-line, Continuous & Batch in solution & Tubular reactor & 2 mm ID, 15 m L & Single-phase & ASA in ethanol & CSD & 779-407-348\%\tnote{a} & 7, 14, 16\% wt \\ \addlinespace
\cite{Eder2012} & In-line, Continuous & US-aided nucleation & Tubular reactor & 2 mm ID, 27 m L & Two-phase slug flow & ASA in ethanol & CSD & 172-700\% \tnote{a} & Based on relative flow rate \\ \addlinespace
\cite{Jiang2014} & In-line, Continuous & Micromixing (cooling) & Tubular reactor & 3.1 mm ID, 15.2 m L & Two-phase slug flow & LAM in water & No & 87\%\tnote{b} & / \\ \addlinespace
\cite{Jiang2015} & In-line, Continuous & US-aided nucleation & Tubular reactor & 3.1 mm ID, 15.2 m L & Two-phase slug flow & LAM in water & No & 74\%\tnote{b} & / \\ \addlinespace
\cite{Jordens2017} & In-line, Semi-continuous & US-aided nucleation and growth & Tubular nucleation + batch growth & 5 mm ID, 7 m L tubular nucleation 53x83x97 mm batch vessel & Single-phase & PCM in water & No & No & / \\ \addlinespace
\cite{Wong2013} & In-line, Continuous & Single crystal contact nucleation & Nucleator + tubular reactor & 3.2 mm ID 20 ft L & Single-phase & Glycine/ PCM in water & CSD & No & Single crystal \\ \addlinespace
\cite{MendezDelRio2006} & In-line, Continuous & Cooling & Tubular nucleation (LFTC) + batch growth & 1.6 mm ID, 7.62 m L LFTC 500 ml batch vessel & Single-phase & PCM in ethanol/ methanol & No & No & / \\ \addlinespace
\cite{Fatemi2021} & In-line, Continuous & Cooling & Tubular microreactor + tubular growth & 1 mm ID, 60 cm L tubular nucleation 2 mm ID, 1.4, 4, 8 m L tubular growth & Two-phase bubble flow & PCM in water & No & 2-70\% \tnote{c} & / \\
\end{xltabular}
\end{ThreePartTable}
\end{landscape}
\end{document}